ILLINOIS POLLUTION CONTROL
BOARD
December 19,
1991
IN THE
MATTER
OF:
)
R91—13
RCRA UPDATE, USEPA REGULATIONS)
)
Identical in Substance
(1/1/91
—
6/30/91)
)
Rules)
PROPOSAL FOR PUBLIC COMMENT
PROPOSED
ORDER
OF THE BOARD
(by J. Anderson):
By a separate Order, pursuant to Section 7.2 and 22.4(a)
of
the Environmental Protection Act
(Act), the Board is proposing to
amend the RCRA hazardous waste regulations.
The amendments
involve 35 Ill. Adm. Code 703, 720,
721,
722,
724,
725,
726 and
728.
The Board will receive public coirinent for 45 days after the
date of publication of the proposed rules in the Illinois
Register.
The complete text of the Proposed rules
is attached to this
Order.
Because of its length, the text will not appear in the
Environmental Register,
or the Opinions volumes.
However, the
text will be mailed to persons on the notice
list,
and will
appear in the Illinois Register shortly.
IT IS SO ORDERED.
I, Dorothy H. Gunn,
Clerk of the Illinois Pollution Control
Board, her~bycertify that the above Proposed Order was adopted
on the
/P—
day of
/~‘~
,-n4~_’
,
1991,
by a vote of
~
/~
Dorothy N. Gu~(,Clerk
Illinois Politition Control Board
128—469
2
TITLE
35:
ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
b:
PERMITS
PART
703
RCRA PERMIT PROGRAM
SUBPART
A:
GENERAL
PROVISIONS
Section
703.100
703.
101
703.110
Scope and Relation to Other Parts
Purpose
References
SUBPART B:
PROHIBITIONS
Prohibitions in General
RCRA Permits
Specific Inclusions in Permit Program
Specific Exclusions from Permit Program
Discharges of Hazardous Waste
Reapplications
Initial Applications
Federal Permits
(Repealed)
SUBPART C:
AUTHORIZATION BY RULE
AND
INTERIM STATUS
Section
703.140
703.141
703.150
703.151
703.152
703.153
703.154
703.155
703.156
703. 157
703.158
703.159
703.
160
Section
703.180
703.181
703.182
703.183
703.184
703.185
703.186
.703.187
Purpose and Scope
Permits by Rule
Application by Existing HWN Facilities and Interim
Status Qualifications
Application by New HWN Facilities
Amended Part A Application
Qualifying for Interim Status
Prohibitions During Interim Status
Changes During Interim Status
Interim Status Standards
Grounds for Termination of Interim Status
Permits for Less Than an Entire Facility
Closure by Removal
Procedures for Closure Determination
SUBPART D:
APPLICATIONS
Applications in General
Contents of Part A
Contents of Part B
General Information
Facility Location Information
Groundwater Protection Information
Exposure Information
Solid Waste Management Units
Section
703.120
703.121
703.122
703.123
703.124
703~125
703.126
703
.
127
128—470
3
703.188
703.200
703.201
703.202
703.203
703.204
703.205
703.206
703.207
703.208.
703.209
703.210
703.211
703.212
Section
703.221
703.222
703.223
703.224
703.225
703.230
703.231
703.232
Other Information
Specific Information
Containers
Tank Systems
Surface Impoundments
Waste Piles
Incinerators
Land Treatment
Landfills
SDecific Part B Information Reauirements for Boilers
and Industrial Furnaces
Miscellaneous Units
Process Vents
Equipment
Drip Pads
SUBPART E:
SHORT TERM
AND
PHASED PERMITS
Emergency Permits
Incinerator Conditions Prior to Trial Burn
Incinerator Conditions During Trial Burn
Incinerator Conditions After Trial Burn
Trial Burns for Existing Incinerators
Land Treatment Demonstration
Research, De~relopmentand Demonstration Permits
Permits for Boilers and Industrial Furnaces Burning
Hazardous Waste
SUBPART F:
PERMIT CONDITIONS OR DENIAL
Permit Denial
Establishing Permit Conditions
Noncompliance Pursuant to Emergency Permit
Monitoring
Notice of Planned Changes
Twenty-four Hour Reporting
Reporting Requirements
Anticipated Noncompliance
SUBPART
G:
CHANGES
TO
PERMITS
Transfer
Modification
Causes for Modification
Causes for Modification or Reissuance
Facility Siting
Permit Modification at the Request of the Permittee
Class
1 Modifications
Class
2 Modifications
Class
3 Modifications
Appendix A
Classification of Permit Modifications
Section
703.240
703.241
703.242
703.243
703
.
244
703.245
703.246
703.247
Section
703.260
703.270
703.271
703.272
703.273
703.280
703 .281
703.282
703.283
12
8—47
1
4
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
111½, pars. 1022.4 and 1027).
SOURCE:
Adopted in R82-19,
53 PCB 131, at 7 Ill. Reg.
14289,
effective October 12,
1983; amended in R83—24 at 8
Ill.
Reg. 206,
effective December 27,
1983; amended in R84-9 at 9
Ill.
Reg.
11899, effective July 24,
1985; amended in R85—22 at 10 Ill. Reg.
1110, effective January
2,
1987; amended in R85—23 at 10 Ill.
Reg. 13~84,effective July 28,
1986; amended in R86—1 at 10 Ill.
Reg.
14093,
effective August 12, 1986; amended in R86—19 at 10
Ill. Reg.
20702, effective December 2,
1986; amended in R86-28 at
11 Ill. Reg.
6121, effective March 24,
1987; amended in R86-46 at
11 Ill. Reg.
13543,
effective August 4,
1987;
amended in R87—5 at
11
ill.
Reg.
19383,
effective November 12,
1987; amended in R87-
26
at
12
Ill.
Reg.
2584,
effective
January
15,
1988;
amended
in
R87—39
at
12
Ill.
Reg.
13069,
effective
July
29,
1988;
amended
in
R88—16
at
13
Iii.
Reg.
447,
effective
December
27,
1988;
amended
in
P29-i
at
13
Ill.
Reg.
18477,
effective
November
13,
1989;
amended
in
R89—9
at
14
Ill.
Reg.
6278,
effective
April
16,
1990;
amended
in
R90-2
at
14
Ill.
Reg.
14492,
effective
August
22,
1990;
amended
in
R90—11 at 15
Ill.
Reg.
9616,
effective
June
17,
1991;
amended
in
R91—1
at
15
Ill.
Reg.
14554,
effective October
1,
1991;
amended
in
R91—13
at
16
Ill
Reg.
,
effective
SUBPART
C:
AUTHORIZATION BY RULE AND INTERIM STATUS
Section
703.150
Application
by
Existing
HWM
Facilities
and
Interim
Status
Qualifications
a)
The
owner
or
operator
of
an
existing
11W)!
facility
or
of
an
11W)! facility in existence on the effective date of
statutory
or
regulatory
amendments
that
render
the
facility
subject
to
the
requirement to have a RCRA
permit must submit Part A of the permit application to
the Agency no later than the following times, whichever
comes first:
1)
Six months after the date of publication of
regulations which first require the owner or
operator to comply with standards in 35 Ill.
Adin.
Code 725 or 726 or
2)
Thirty days after the date the owner or operator
first becomes subject to the standards in 35 Ill.
Adin. Code 725 or 726
3)
For generators which generate greater than 100
kilograms but less than 1000 kilograms of
hazardous waste in a calendar month and treat,
128—472
5
store or dispose of these wastes on—site, by March
24,
1987.
BOARD NOTE:
Derived from 40 CFR 270w 10(e~(1) and
270.1(b)
(1991), amended at 56 Fed. Req.
32688,
July 17. 1991.
The owner or operator of an cxioting
11W)! facility may
be required to submit Part B of the permit application
—
at any time atter tne errcctive pace
~.
otgndard3.in 35
Ill. Adm. Code 724 applicabic to any TCD unit at the
facility.
The Aqcncv uill notify the owner or operatni
that
~
i-~
~rnr~~is-
is required-
ririti
~i~t
—
y-
i
r’~
~
1
n
for
...~iptof the ~
~.
L~
after the date the notice
i...
...~
~
‘
~p1icati
uij.
or part of the 11W)! fpcility at ~ny time.
~fl
granting a variance under subsection
(C). the Board
will consider whether there has been substantial
confusion as to whether the owner or operator of such
facilities
were
required
to
file
a
Part
A
application
and whether such confusion was attributable to
ambiguities
in
35
Ill. Adm. Code 720, 721 or 725.
operritnr
—“
vcjunt~iri
sent.
mt.
--
nfl
for
i
~_
.~
Part
BOARD
NOTE:
Derived
from
40
CFR
270.10(e)(2)
(1990).
c)
The
time
for
filing
Part
A
of
the permit application
may
be
extended
only
by
a
Board
Order
entered pursuant
to
a
variance
petition.
The
Board will conaider
whether there has been substantial confuoion go to
wnecner cne owner or operator ot ~ucn
racLlJ.cies
were
required to file a Part A application and whether such
confusion was attributable to ambiguities in 35
Iii.
Adm. Code 720,
721 or 725.
BOARD NOTE:
Derived from 40 CFR 270.10(e) (3)
(1990).
d)
The owner or operator of an existing
HWM
facility
may
be required to submit Part B of the permit application
at any time after the effective date of standards in 35
Ill. Adm.
Code 724 applicable to any TSD unit at the
facility.
The Agency will notify the owner or operator
that a Part B application is required, and set a date
for receipt of the application, not less than six
months after the date the notice
is sent. The owner or
operator my voluntarily submit. a Part B application for
all or part of the
11W)! facility at any time.
Notwithstanding the above,
any owner or operator of an
existing HWM facility must submit a Part B permit
application in accordance with the dates specified in
Section 703.157.
Any owner or operator of
a land
disposal
facility
in existence on the effective date of
b)
128—473
6
statutory or regulatory amendments which render the
facility subject to the requirement to have a RCRA
permit must submit a Part B application in accordance
with the dates specified in Section 703.157.
BOARD NOTE:
Derived from 40 CFR 270.10(e) (4)
(1990).
e)
Inter~imstatus may be terminated as provided in Section
703. 157.
BOARD NOTE:
Derived from 40 CFR 270.10(e) (5)
(1990).
(Board Note:
Cee 40 CFR 270.10(c).)
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
Section 703.155
Changes During Interim Status
a)
Except as provided in subsection
(b), the owner or
operator of an interim status facility may make the
following changes at the facility:
1)
Treatment, storage or disposal of new hazardous
wastes not previously identifled in Part A of the
permit application
(and,
in the case of newly
listed or identified wastes, addition of the units
being used to treat, store or dispose of the
hazardous wastes on the date of the listing or
identification)
if the owner or operator submits a
revised Part A permit application prior to such
treatment, storage or disposal;
2)
Increases in the design capacity of processes used
at the facility if the owner or operator submits a
revised Part A permit application prior to such a
change
(along with a justification explaining the
need for the change) and the Agency approves the
change because:
A)
There is a lack of available treatment,
storage or disposal capacity at other
hazardous waste management facilities; or
B)
The change is necessary to comply with a
federal,
State or local requirement,
including 35 Ill. Adm. Code 725,
728 or 729.
3)
Changes in the processes for the treatment,
storage or disposal of hazardous waste may be made
at a facility or addition of processes may be
added if the owner or operator submits a revised
128—4
74
7
Part A permit application prior to such a change
(along with a justification explaining the need
for change) and the Agency approves the change
because:
A)
The change is necessary to prevent a threat
to human health or the environment because of
an emergency situation; or
B)
The change is necessary to comply with a
Federal, State or local requirement,
including 35 Ill.
Adm. Code 725, 728 or 729;
4)
Changes in the ownership or operational control of
a facility if the new owner or operator submits a
revised Part A permit application no later than 90
days
prior
to the scheduled change.
When a
transfer
of
ownership
or
operational control of a
facility occurs, the old owner or operator shah
comply with the requirements of 35 Ill.
Adiu. Code
725..Subpart H (financial requirements), until the
new owner or operator has demonstrated to the
Agency that it is complying with the requirements
of
that
Subpart.
The new owner or operator shall
demonstrate
compliance
with
the financial
assurance
requirements
within
six
months
after
the
date
of
the
change
in
the
ownership or operational
control
of
the
facility.
Upon
demonstration
to
the Agency by the new owner or operator of
compliance with the financial assurance
requirements, the Agency shall notify the old
owner or operator in writing that the old owner or
operator no longer needs to comply with 35 Ill.
Adm. Code 725..Subpart H as of the date of
demonstration.
All
other
interim
status
duties
are transferred effective immediately upon the
date of the change of ownership or operational
control
of the facility;
5)
Changes
made
in
accordance
with
an
interim
status
corrective
action
order
issued
by:
USEPA
under
Section 3008(h) of the Resource Conservation and
Recovery Act or other federal authority;
a court
pursuant to a judicial actjon brought USEPA;
a
court pursuant to the Environmental Protection
Act;
or, the Board.
Changes under this subsection
are limited to the treatment,
storage or disposal
of solid waste from releases that originate within
the boundary of the facility.
~j.
Addition of newly regulated units for the
treatment,
storage
or disposal of hazardous waste
128—475
8
if the owner or operator submits
a revised Part A
permit application on or before the date on which
the unit becomes subiect to the new requirements.
b)
Except as specifically allowed under this subsection,
changes listed under subsection
(a) must not be made if
they amount to reconstruction of the HWM facility.
Reconstruction occurs when the capital investment in
the changes to the facility exceeds fifty percent of
the capital cost of a comparable entirely new HWM
facility.
If all other requirements are met, the
following changes may be made even if they amount to a
reconstruction:
1)
Changes made solely for the purposes of complying
with requirements of 35
Ill. Adm. Code 725.293 for
tanks and ancillary equipment.
2)
If necessary to comply with federal, State or
local requirements, including 35 Ill.
Adm. Code
725, 728 or 729, changes to an existing unit,
changes solely involving tanks or containers,
or
addition of replacement surface impoundments that
satisfy the statutory standards of Section 35
Iii.
Adin. Code 728.139.
3)
Changes that are necessary to allow owners or
operators to continue handling newly listed or
identified hazardous wastes that have been
treated,
stored or disposed of at the facility
prior to the effective date of the rule
establishing the new listing or identification.
4)
Changes during closure of a facility or of a unit
within a facility made in accordance with an
approved closure plan.
5)
Changes necessary to comply with an interim status
corrective action order issued by:
USEPA under
Section 3008(h)
of the Resource Conservation and
Recovery Act or other federal authority.;
a ,court
pursuant to a judicial action brought by USEPA;
a
court pursuant to the Environmental Protection
Act;
or, the Board.
Changes under this subsection
are limited to the treatment, storage or disposal
of solid waste from releases that originate within
the boundary of the facility.
6)
Changes to treat or store,
in tanks or containers,
hazardous wastes subject to land disposal
restrictions imposed in 35 111.
Adin.
Code 728,
provided that such changes are made solely for the
128—476
9
purpose of complying with 35 Ill. Adm. Code 728.
21
Addition of newly regulated units under subsection
(a) (6).
(Board Note:
Derived from 40 CFR 270.72
-(1980),
as aincnaea at 54 Fea.
fleg.
9607, Marcn
7,
1989(1990.
as amended 56 Fed. Req. 7206.
February
21
1991.)
(Source:
Amended at 16
Ill. Reg.
,
effective
)
Section 703.157
Grounds for Termination of Interim Status
Interim
status
terminates
when:
a)
Final administrative disposition of a permit
application is made;
or
b)
The owner or operator fails to furnish a requested Part
B application on time, or to furnish the full
information required by the Part B application,
in
which case the Agency shall notify the owner and
operator of the termination of interim status following
the procedures for a notice of intent to deny a permit
pursuant to 35 Ill. Adm. Code 705.
c)
For owners or operators of each land disposal facility
which has been granted interim status prior to November
8,
1984, on November 8,
1985,
unless:
1)
The owner or operator submits a Part B application
for a permit for such facility prior to that date;
and
2)
The owner or operator certifies that such facility
is in compliance with all applicable groundwater
monitoring and financial responsibility
requirements.
d)
For owners or operators of each land disposal facility
which is in existence on the effective date of
statutory or regulatory amendments under the Resource
Conservation and Recovery Act that render the facility
subject to the requirement to have a RCRA permit and
which is granted interim status, twelve months after
the date on which the facility first becomes subject to
such permit requirement unless the owner or operator of
such
facility:
1)
Submits a Part B application for a RCRA permit for
128—479
10
such facility before the date 12 months
after
the
date on which the facility first becomes subject
to such permit requirement; and
2)
Certifies that. such facility is in compliance with
all applicable groundwater monitoring and
financial responsibility requirements.
e)
For owners or operators of any land disposal unit that
is granted authority to operate under Section
703.155(a) (1),
(2) or
(3), on the day 12 months after
the effective date of such requirement, unless the
owner or operator certifies that such unit is in
compliance with all applicable groundwater monitoring
and financial responsibility requirements.
(35 Ill.
Adm. Code 725.190 et seq. and 725.240 et seq.)
f)
For owners and operators of each incinerator facility
which achieved interim status prior to November 8,
1984.
interim status terminates on November 8,
1989,
unless the owner or operator of the facility submits a
Part B application for aRCRA permit for an incinerator
facility by November 8,
1986.
g)
For owners and operators of any facility
(other than a
land disposal or an incinerator facility) which
achieved interim status prior to November 8
1984,
interim status terminates on November 8,
1992,
unless
the owner or operator of the facility submits a Part B
application for a RCRA permit for the facility by
November 8,
1988.
(Board Note:
Derived from 40 CFR 270.10(e) (5)
(19831990)
and 270.73
(1980), as amended at 54
Fed.
Rcg.
9G07, March 7,
19091990,
as amended at 56
Fed.
Req.
7206, February 21. 1991.)
(Source:
Amended at 16 Ill. Reg.
,
effective
SUBPART D:
APPLICATIONS
Section 703.208
Specific Part B Information Requirements for
Boilers and Industrial Furnaces
~j
Trial burns.
fl
General.
Except as provided below,
owners and
operators that are subiect to the standards to
control organIc emissions provided by
35
Ill.
Adm. Code 726.204, standards to control
particulate matter provided by 35 Ill. Adm. Code
128—480
11
726.205 standards to control metals emissions
provided by 35 Ill. Adm.
Code 726.206, or
standards to control hydrogen chloride
(HC1) or
chlorine gas emissions provided by 35
Ill.
Adxn.
Code 726.207 shall conduct a trial burn to
demonstrate conformance with those standards and
shall submit a trial burn plan or the results of a
trial burn,
including all required determinations,
in accordance with Section 703.232.
~
Under subsection
(a) (2)
—
(5) and 35 Ill.
Adm. Code 726.204
—
726.207. the Agency may
waive a trial burn to demonstrate conformance
with_a_particular emission standard; and
~j
The owner or operator may submit date in lieu
of a trial burn,
as prescribed in
subsection
(a) (6).
~
Waiver
of
trial
burn
of
DRE
(destruction
removal
efficiency).
~j
Boilers
operated
under
special
operating
requirements.
When
seeking
to
be
permitted
under
35 Ill. Adm. Code 726.204
(a) (4)
and
726.220
that
automatically
waive
the
DRE
trial
burn,
the
owner
or
operator of a boiler
shall
submit
documentation
that
the
boiler
operates under the special operating
requirements provided by 35 Ill. Adm. Code
726. 220
~j
Boilers and industrial furnaces burning low
risk waste.
When seeking to be permitted
under
the provisions for low risk waste
provided by 35 Ill.
Adm. Code
726.204(a)(5)
and 726.209(a)
that waive the DRE trial burn,
the owner
or operator shall submit:
j).
Documentation that the device is
operated in conformance with the
requirements of 35 Ill. Adm. Code
726.209 (a) (1).
ijI
Results of analyses of each waste to be
burned, documenting the concentrations
of nonmetal compounds listed in 35
Ill.
Adm. Code 721.Appendix H. except for
those constituents that would reasonably
not
be
expected
to
be
in
the
waste.
The
constituents excluded from analysis must
be
identified
and the basis for their
128—48
1
12
exclusion explained.
The analysis must
rely on analytical techniques specified
in Test Methods for the Evaluation of
Solid Waste, Physical/Chemical Methods
(incOrporated by reference,
see 35
Ill.
Adm.
Code 720.111)
iii) Documentation of hazardous waste firing
rates and calculations of reasonable.
worst—case emission rates of each
constituent identified subsection
(a) (1) (B)
(ii)
using procedures provided
by 35 Ill.
Adm. Code 726.209(a) (2) (B).
jyJ.
Results of emissions dispersion modeling
for emissions identified in subsection
(a) (2) (B) (iii) using modeling procedures
prescribed by 35
Ill.
Adin. Code
726.206(h).
The Agency shall review the
emission modeling conducted by th~
applicant to determine conformance with
these procedures.
The Agency shall
either approve the modeling or determine
that alternate or supplementary modeling
is appropriate.
yl
Documentation that the maximum annual
average ground level concentration of
each constituent identified
in
subsection
(a) (2) (B)
(ii)
quantified in
conformance with subsection
(a) (2) (B) (iv) does not exceed the
allowable ambient level established in
35 Ill.
Adin. Code 726.Appendices D or E.
The acceptable ambient concentration for
emitted constituents for which a
specific reference air concentration has
not_been established in 35 Ill.
Adm.
Code 726.Appendix D or risk-specific
does has not been established in 35
Ill.
Adm._Code 726.Appendix E is 0.1
micrograms per cubic meter. as noted in
the footnote to 35 Ill. Adm. Code
726.Appendix D.
fl
Waiver of trial burn for metals.
When seeking to
be permitted under the Tier I
(or ad-justed Tier I)
metals feed rate screening limits provided by 35
Ill. Adm. Code 726.206(b)
and
(c) that control
metals emissions without requiring a trial burn,
the owner or operator shall submit:
128—482
13
~
Documentation of the feed rate of hazardous
waste, other fuels and industrial furnace
feed stocks
~j
Documentation of the concentration of each
metal controlled by 35 Ill.
Adm..
Code
726.206(b)
or
(e)
in the hazardous waste,.
other fuels and industrial furnace
feedstocks. and calculations of the total
feed rate of each metal
~
Documentation of how the applicant will
ensure that the Tier
I feed rate screening
limits provided by 35 Ill. Adm. Code
726.206(b)
or
(e) will not be exceeded during
the averaging period provided by thai
subsection
Qj
Documentation to support the determination of
the TESH (terrain-adlusted effective stack
height).
aood engineering practice stack
height,
terrain
type
and land use as provided
by 35 Ill. Adm. Code 72,6.206(b) (.3)
—
(5
)
~j
Documentation
of
compliance
with
the
provisions
of
35
Ill. Adm. Code
726.206(b) (6),
if
applicable,
for
facilities
with multiple stacks
fi
Documentation that the facility does not fail
the criteria provided by 35 Ill. Adm. Code
726.206(b) (7)
for eligibility to comply with
the screening limits; and
~j.
Proposed sampling and metals analysis plan
for the hazardous waste,
other fuels and
industrial furnace feed stocks.
j)
Waiver of trial burn for PM
(particulate matter).
When seeking to be permitted under the low risk
waste provisions of 35 Ill.
Adm. Code 726.209(b)
which waives the particulate standard (and trial
burn_to_demonstrate conformance with the
particulate standard),
applicants shall submit
documentation supporting conformance with
subsection
(a) (21 (B) and
(3).
.~j.
Waiver of trial burn for HC1 and chlorine gas.
When seeking to be permitted under the Tier I
(or
adjusted Tier I) feed rate screening limits for
total chlorine and chloride provided by 35 Ill.
Adm. Code 726.207(b) (1)
and
(e) that control
128—483
14
emissions by MCi and chlorine gas without
reguiring a trial burn, the owner or oPerator
shall submit:
~
Documentation of the feed rate of hazardous
waste.
other fuels, and industrial furnace
feed stocks
~j
Documentation of the levels of total chlorine
and chloride in the hazardous waste,
other
fuels and industrial furnace feedstocks’.
and
calculations of the total feed rate of total
chlorine and chloride
QI
Documentation of how the applicant will
ensure that the Tier
I
(or ad-justed Tier
I)
feed rate screening limits provided by 35
Ill.
Adm.
Code
726.207(b)
(1)
or
(e)
will
not
be exceeded during the averaging period
provided by that subsection
QJ
Documentation to su~~ortthe determination of
the TESH.
good engineering practice stack
height, terrain type and land use as provided
bsr35 Ill. Adm. Code 726.207(b) (3).
.~j
Documentation of compliance with the
provisions of 35 Ill. Adm. Code
726.207(b) (41,
if applicable,
for facilities
with multiple stacks
fi
Documentation that the facility does not fail
the criteria provided by 35 Ill.
Adm. Code
726.207(b) (3) for eligibility to comply with
the screening limits; and
Qj
Proposed sampling and analysis plan for total
chlorine and chloride for the hazardous
waste, other fuels,
and industrial furnace
feedstocks.
Qj
Data in lieu of trial burn.
The owner or operator
may seek an exemption from the trial burn
requirements to demonstrate conformance with
Section 703.232 and 35 Ill.
Adm. Code 726.204—
726.207 by providing the information required by
Section 703.232 from previous compliance testing
of the device in conformance with 35 Ill. Adm.
Code
726.203. or from compliance testing or trial
or operational burns of similar boilers or
industrial furnaces burning similar hazardous
wastes under similar conditions.
If data from a
128—484
15
similar device is used to support a trial, burn
waiver, the design and operating information
required by Section 703.232 from previous
compliance testing of
the. device in conformance
with 35 Iii. Mm.
Code 726.203. or from compliance
testing or trial or operational burns of similar
boilers or industrial furnaces burning similar
hazardous wastes under similar conditions.
If
data from a similar device is used to su~~ort
a
trial burn waiver, the design and operating
information
required
by
Section
703.232
must
be
provided for both the similar device and the
device to which the data is to be applied, and a
comparison of the
design
and operating information
must be provided.
The Agency shall approve a
permit application without a trial burn if he
finds that the hazardous wastes are sufficiently
similar,
the devices are sufficiently similar, the
operating conditions are sufficiently similar, and
the data from other compliance tests,
trial burns,
or operational burns are adequate to specify
(under 35
Ill. Adm. Code 726.102)
operating
conditions that will ensure conformance with 35
Ill.
Adm. Code 726.102(c).
In addition, the
following information shall be submitted:
~
For a waiver from any trial burn:
il
A description and analysis of the
hazardous waste to be burned compared
with the hazardous waste for which data
from compliance testing or operational
or trial burns are provided to support
the contention that a trial burn is not
needed
iLL
The design and operating conditions of
the boiler or industrial furnace to be
used, compared with that for which
comparative burn data are available: and
iii) Such supplemental information as the
Agency finds necessary to achieve the
purposes of this subsection.
~j
For a waiver of the DRE trial burn,
the basis
for selection of POHCs (principal organic
hazardous constituents) used in the other
trial or operational burns which demonstrate
compliance with the DRE performance standard
in 35 Ill. Adm. Code 726.204
(a).
This
analysis should specify the constituents in
128—485
16
35
Ill.
Adm.
Code
72l.Appendix
H,
that
the
applicant has identified in the hazardous
waste for which a permit is sought, and any
differences from the POHCs
in the hazardous
waste
for. which burn data are provided.
~j
Alternative’HC limit for industrial furnaces with
organic matter in raw materials.
Owners and operators
of industrial furnaces requesting an alternative HC
limit under 35 Ill. Adm. Code 726.204(f)
shall submit
the_following information at a minimum:
flU.
Documentation that the furnace is designed and
operated to minimize HC emissions from fuels and
raw materials
21
Documentation of the proposed baseline flue gas MC
(and CO) concentration, including data on HC (and
CO)
levels during tests when the facility produced
normal products under normal operating conditions
from normal raw materials while burning normal
fuels and when not burning hazardous waste
,~j,..
Test burn protocol to confirm the baseline MC
(and
CO)
level including information on the type and
flow rate of all feedstreams. point of
introduction of all feedstreams. total organic
carbon content
(or other appropriate measure of
organic content)
of all nonfuel feedstreams, and
operating conditions that affect combustion of
fuel(s) and destruction of hydrocarbon emissions
from nonfuel sources
4j
Trial burn plan to:
~j
Demonstrate that flue gas HC (and CO)
concentrations when burning hazardous waste
do not exceed the baseline HC
(and CO) level
and
~j.
Identify,
in conformance with Section
703.232(d). the types and concentrations of
organic compounds listed in 35 Ill. Adm. Code
721.Appendix H that are emitted when burning
hazardous waste
~
Implementation plan to monitor over time changes
in the operation of the facility that could reduce
the baseline MC level and procedures to
periodically confirm the baseline MC level; and
j)
Such other information as the Agency finds
128—486
17
necessary to achieve the purposes of this
subsection.
~j,
Alternative metals implementation approach.
When
seeking to be permitted under an alternative metals
implementation approach under 35 Ill.
Adm. Code
726.206(f), the owner or operator shall submit
documentation specifying how the a~~roachensures
compliance with the metals emissions standards of 35
Ill. Adm. Code 726.106(c)
or
(dl and how the approach
can be effectively implemented and monitored.
Further,
the owner or operator shall provide such other
information that the Agency finds necessary to achieve
the purposes of this subsection.
~,j
Automatic waste feed cutoff system.
Owners and
operators shall submit information describing the
automatic waste feed cutoff system,
including any pre-
alarm systems that may be used.
~j
Direct transfer.
Owners and operators that use direct
transfer operations to feed hazardous waste from
transport vehicles
(containers, as defined in 35 Ill.
Mm. Code 726.211) directly to the boiler or industrial
furnace shall submit information supporting conformance
with the standards for direct transfer provided by 35
Ill.
Adm. Code 726.211.
fj.
Residues.
Owners and operators that claim that their
residues are excluded from regulation under the
provisions of 35
Ill. Adm. Code 726.212 shall submit
information adeguate to demonstrate conformance with
those provisions.
(Source:
Added at 16
Ill. Reg.
,
effective
)
Section 703.211
Equipment
Except as otherwise provided in 35 Ill. Adm. Code 724.101, owners
and operators of facilities which have equipment to which 35 Ill.
Adm. Code 724.Subpart BB applies shall provide the following
additional information:
a)
For each piece of equipment to which 35 Ill. Adm. Code
724.Subpart BB applies:
1)
Equipment identification number and hazardous
waste management unit identification.
2)
Approximate locations within the facility
(e.g.,
identify the hazardous waste management unit on a
128—487
18
facility plot plan).
3)
Type
of
equipment
(e.g.,
a
pump
or
pipeline
valve).
4)
Percent by weight total organics in the hazardous
wastestream at the equipment.
5)
Hazardous waste state at the equipment (e.g.,
gas/vapor or liquid).
6)
Method of compliance with the standard (e.g.,
“monthly leak detection and repair” or “equipped
with dual mechanical seals”).
b)
For facilities which cannot install a closed-vent
system and control device to comply with 35 Ill. Adm.
Code 724.Subpart BB on the effective date that facility
becomes subject to this Subpart or 35 Ill. Adm. Code
724.Subpart BB, an implementation schedule as sp~cified
in 35 Ill. Adm. Code 724.933(a) (2).
C)
Where an owner or operator applies for permission to
use a control device other than a thermal vapor
incinerator, ‘catalytic vapor incinerator, flare,
boiler, process heater, condenser or carbon adsorption
system and chooses to use test data to determine the
organic removal efficiency or the total organic
compound concentration achieved by the control device,
a performance test plan as specified in 35 Ill. Adm.
Code 724.935(b) (3)
d)
Documentation which demonstrates compliance with the
equipment standards in 35 Ill. Adm. Code 724.952 or
724.959.
This documentation must contain the records
required under
35 Ill. Adm. Code 724.964.
The Agency
shall request further documentation if necessary to
demonstrate compliance.
Documentation to demonstrate
compliance with 35 Ill. Adm. Code 724.960 must include
the following information:
1)
A list of all information references and sources
used in preparing the documentation.
2)
Records~including the dates of each compliance
test required by 35 Ill. Adm. Code 724.933(j).
3)
A design analysis, specifications,
drawings,
schematics, and piping and instrumentation
diagrams based on the appropriate sections of APTI
Course 415, incorporated by reference in 35 Ill.
Adm. Code 720.111, or other engineering texts
128—488
19
appproved by the Agency which present basic
control device design information.
The design
analysis must address the vent stream
characteristics and control device parameters as
specified in 35
Ill. Adm. Code 724.935(b) (4) (C.
4)
A statement signed and dated by the owner or
operator certifying that the operating parameters
used in the design analysis reasonably represent
the conditions which exist when the hazardous
waste management unit is or would be operating at
the highest load or capacity level reasonably
expected to occur.
5)
A statement signed and dated by the owner or
operator certifying that the control device is
designed to operate at an efficiency of 95 weight
percent or greater.
(Source:
Amended at 16
Ill. Reg.
,
effective
)
SUBPART E:
SHORT TERN AND
PHASED PERMITS
Section 703.232
Permits for Boilers and Industrial Furnaces
Burning Hazardous Waste
,~j,
General.
Owners and operators of new boilers and
industrial furnaces
(those not operating under the
interim status standards of
35 Ill. Adm. Code 726.203)
are subiect to subsection
(b)
—
(f).
Boilers and
industrial furnaces operating under the interim status
standards of 35
Ill. Adm. Code 726.203 are subject to
subsection
(g).
~j
Permit operating periods for new boilers and industrial
furnaces.
A permit for a new boiler or industrial
furnace must specify appropriate conditions for the
following operating periods:
fl
Pretrial burn period.
For the period beginning
with initial introduction of hazardous waste and
ending with initiation of the trial burn,
and only
for the minimum time required to bring the boiler
or industrial furnace to a point of operation
readiness to conduct a trial burn,
not to exceed
720 hours operating time when burning hazardous
waste,
the Agency shall establish in the Pretrial
Burn Period of the permit conditions,
including
but not limited to allowable hazardous waste feed
rates and operating conditions.
The Agency shall
extend the duration of this operational period
128—489
20
once, for up to 720 additional hours, at the
request of the applicant when good cause is shown.
The permit most be modified to reflect the
extension according to Section 703.280 et seq.
Aj
Applicants must submit p statement, with part
B of the permit application, that suggests
the conditions necessary to operate in
compliance with the standards of 35
Ill.
Adm.
Code 726.204—726.207 during this period.
This statement should include, at a minimum,
restrictions on the applicable operating
requirements identified in 35
Ill. Adm. Code
726.202
(e).
~j
The Agency shall review this statement and
any other relevant information submitted with
part B of the permit application and specify
requirements for this period sufficient to
meet the performance standards of 35 Ill.
Adin.
Code 726.204—726.207 based on the
Agency’s engineering -judgment.
21
Trial burn period.
For the duration of the trial
burn, the Agency shall establish conditions in the
permit for the purposes of determining feasibility
of compliance with the performance standards of
35
Ill.
Adin. Code 726.204—726.207 and determining
adequate operating conditions under 35 Ill. Adm.
Code 726.202
(e).
Applicants shall propose a
trial burn plan, prepared under subsection
(c), to
be submitted with part B of the permit
application.
fl
Post-trial burn period.
~j.
For
the
period
immediately
following
completion of the trial burn,
and only for
the minimum period sufficient to allow sample
analysis, data computation and submission of
the trial burn results by the applicant,
and
review of the trial burn results and
modification of the facility permit by the
Agency to reflect the trial burn results,
the
Agency shall establish the operating
requirements most likely to ensure compliance
with the performance standards of 35 Ill.
Ads. Code 726.204-726.207 based on the
Agency’s engineering -judgment.
~j
Applicants shall submit
a statement, with
part B of the application, that identifies
128—490
21
the conditions necessary to operate during
this period in compliance with the
performance standards of 35
Ill.
Ads. Code
726.204—726.207.
This statement should
include, at a minimum, restrictions on the
operating requirements provided by 35 Ill.
Adm. Code 726.202
(e).
çJ
The Agency shall review this statement and
any other relevant information submitted with
part B of the permit application and specify
requirements of this period sufficient to
meet the performance standards of 35 Ill.
Adm. Code 726.204—726.207 based on the
Agency’s engineering -judgment.
iL
Final permit period.
For the final period of
operation the Agency shall develop operating
requirements in conformance with 35 Ill. Adm. Code
726.202
(e) that reflect conditions in the trial
burn elan and are likely to ensure compliance with
the performance standards of
35 Ill. Adm.
.
Code
726.204—726.207.
Based on the trial burn, results,
the Agency shall make any necessary modifications
to the operating requirements to ensure compliance
with the performance standards.
The permit
modification must proceed according to Section
703.280 et seq.
~j
Requirements for trial burn plans.
The trial burn plan
must include the following information.
The Agency,
in
reviewing the trial burn plan,
shall evaluate the
sufficiency of the information provided and may require
the applicant to supplement this information,
if
necessary, to achieve the purposes of this subsection.
fl
An analysis of each feed stream, including
hazardous waste, other fuels, and industrial
furnace feed stocks, as fired, that includes:
~j
Heating value, levels of antimony, arsenic,
barium, beryllium,
cadmium,
chromium,
lead.
mercury,
silver1 thallium, total
chlorine/chloride and ash
~
Viscosity or description of the physical form
of the feed stream:
21
An analysis of each hazardous waste,
as fired,
including:
~j
An
identification
of
any
hazardous
organic
128—49
1
22
constituents listed in 35 Ill. Adm. Code
721.Appendix
H that are present in the feed
stream,
except that the applicant need not
analyze for constituents listed in App. H
which would reasonably not be expected to be
found in the hazardous waste.
The
cOnstituents excluded from analysis must be
identified at the basis for this exclusion
explained.
The analysis :must be conducted
in accordance with analytical techniques
specified in Test Methods for the Evaluation
of Solid Waste, Physical/Chemical Methods
(incorporated by reference,
see 35 Ill.
Adin.
Code 720.111 or their equivalent.)
flj,.
An approximate quantification of the
hazardous constituents identified in the
hazardous waste, within the precision
produced
by
the
analytical
methods
specified
in Test Methods for the Evaluation of Solid
Waste, Physical/Chemical Methods or other
equivalent.
.~j
A description of blending procedures,
if
applicable,
prior
tofirinq
the
hazardous
waste,
including
a
detailed
analysis
of
the
hazardous waste prior to blending, an
analysis
of
the
material
with
which
the
hazardous waste prior to blending,
an
analysis
of
the
material
with
which
the
hazardous waste is blended, and blending
ratios.
.11
A detailed engineering description of the boiler
or industrial furnace, including:
~j
Manufacturer’s name and model number of the
boiler or industrial furnace:
~j.
Type of boiler or industrial furnace
~J,.
Maximum design capacity in appropriate units
Qj
Description of the Feed system for the
hazardous waste, and as appropriate, other
fuels and industrial furnace feedstocks
~
Capacity of hazardous waste feed system
fi
Description of automatic hazardous waste feed
cutoff system(s); and
128—492
23
Qj
Description of any pollution control system
and
~j). Description of stack gas monitoring and any
pollution control monitoring systems.
4j
A detailed description of ‘sampling and monitoring
procedures including sampling and monitoring
locations
in the system. the equipment to be used,
sampling and monitoring frequency and sample
analysis.
,~j
A detailed test schedule for each hazardous waste
for which the trial burn is planned, including
date(s), duration, quantity of hazardous waste to
be burned, and other factors relevant to the
Agency’s decision under subsection
(6) (2).
~j.. A detailed test protocol,
including, for each
hazardous waste identified, the ranges of
hazardous waste feed rate,
and,
as appropriate,
the feed rates of other fuels and industrial
furnace
feedstocks,
and
any
other
relevant
parameters that may affect the ability of the
boiler or industrial furnace to meet the
performance standards in ‘35 Ill. Adm. Code
726.204—726.207.
21
A
description
of
and
planned
operating
conditions
for
any
emission
control
equipment
that
will
be
used.
~
Procedures
for
rapidly
stopping ;the hazardous
waste
feed
and
controlling
emissions
in the event
of
an
equipment
malfunction.
2J,,
Such
other
information
as
the
Agency
finds
necessary to determine whether to approve the
trial burn plan in light of the purposes of this
subsection
and the criteria in subsection
(b)
(2).
Trial
burn
procedures.
fl
A trial burn must be conducted to demonstrate
conformance with the standards of 35 Ill.
Adm.
Code 726.104—726.107.
21
The Agency shall approve a trial burn plan if the
Agency finds that:
~
The trial burn is likely to determine whether
the boiler or industrial furnace can meet the
128—493
24
performance standards of 35
Ill. Adm. Code
726.104—726.107.
~J.
The trial burn itself will not present an
imminent hazard to human health and the
environment
Qj
The trial burn will help the Agency to
determine operating requirements to be
specified under
35 Ill.
Adm. Code 726.102
(dr and
Qj
The information sought in the trial burn
cannot reasonably be develoned through other
means.
fl
The applicant shall submit to the A~encva
certification that the trial burn has been carried
out in accordance with the a~~rovedtrial burn
plan.
and submit the results of all the
determinations required in subsection
(c).
The
Agency shall, in the trial burn plan,
require that
the submission be made within 90 days after
completion of the trial burn,
or later if the
A~encvdetermines that a later date is acceptable.
il
All data collected during any trial’ burn must be
submitted to the Agency following completion of
the
trial
burn.
,~j
All submissions required by this subsection must
be certified on behalf of the applicant by the
signature of a person authorized to sign
a permit
application or a report under 35 Ill. Adm. Code
702. 126.
,~j.
Special procedures for DRE trial burns.
When
a DRE
trial burn is required under 35 Ill. Adm. Code 726.104,
the Agency shall specify (based on the hazardous waste
analysis data and other information in the trial burn
plan)
as trial Principal Organic Hazardous Constituents
(POHCs) those compounds for which destruction and
removal efficiencies must be calculated during the
trial burn.
These trial POHCS will be specified by the
Agency based on information including the Agency’s
estimate of the difficulty of destroying the
constituents identified in the hazardous waste
analysis, their concentrations or mass in the hazardous
waste
feed,
and.m for hazardous waste containing or
derived from wastes listed in 35 Ill. Ads. Code
721.Subpart
D. the hazardous waste organic
constituent(s)
identified in 35 Ill. Adm. Code
128—494
25
721.A~pendixG as the basis for listing.
~j.
Determinations based on trial burn.
During each
approved trial burn (or as soon after the burn as is
practicable), the applicant shall make the following
determinations:
fl..
A quantitative analysis of the levels of antimony,
arsenic, barium, beryllium, cadmium, chromium,
lead, mercury, thallium,
silver, and
chlorine/chloride, in the feed streams
(hazardous
waste,
other fuels, and industrial furnace
feedstocks):
21
When a DRE trial burn is required under 35
Ill.
Adm. Code 726.204
(a):
~j
A quantitative analysis of the trial POHCs
in
the hazardous waste feed
~j
A quantitative analysis of the stack gas for
the concentration and mass emissions of the
trial
POHC5;
and
Qj
A computation of
(DRE).
in accordance with
the DRE formula specified in 35 Ill. Mm.
Code 726.204
(a).
,~j.
When a trial burn for chlorinated dioxins and
furans is required under 35
Ill. Adm. Code 726.204
(e),
a quantitative analysis of the stack gas for
the concentration and mass emission rate of the
2.3,
7. 8—chlorinated tetra—octa congeners of
chlorinated dibenzo—p—dioxins and furans, and a
computation showing conformance with the emission
standard.
~j
When a trial burn for PM. metals,
or HC1/Chlorine
gas is required under 35 Ill. Adm. Code 726.205,
726.206
(c) or
(d)
or 726.207
(b)
(2) or
(c),
a
auantitative
analysis
of
the
stack
gas
for
the
concentrations and mass emissions of PM, metals,
or MCi and chlorine gas and computations showing
conformance with the applicable emission
performance standards
,~j
When a trial burn for DRE. metals, and
HCI/Chiorine gas is required under 35
Ill. Ads.
Code 726.204
(a), 726.206
(c) or
(dl, or 726.207
(b)
(2) or
(c). a quantitative analysis of the
scrubber water
(if any)..ash residues,
other
residues, and products for the purpose of
128—495
26
estimating the fate of the trial POHCs,
metals,
and chlorine/chloride
~J
An identification of sources of fugitive emissions
and their means of control
fl
A continuous
measurement
of
carbon
monoxide
(CO),
oxygen. and where required, hydrocarbons
(MC),
in
the stack gas: and
fi
Such other information as the Agency specifies as
necessary to ensure that the trial burn will
determine compliance with the performance
standards 35
Ill. Adm. Code 726.204
—
726.207 and
to establish the operating conditions required by
35 Ill. Adm. Code 726.204
—
726.207 and of
determining adequate operating conditions under
35
Ill. Adm. Code 726.203,
and to establish the
operating conditions required by 35
Iii.
Adm. Code
726.202
(e)
as necessary to meet those performance
standards.
gj
Interim status boilers and industrial furnaces,
for
the purpose of determining feasibility of compliance
with the performance standards of 35 Ill.
Adm. Code
726.204
-
726.207 and of determining adeauate operating
conditions under 35 Ill. Adm. Code 726.203, applicants
owning or operating existing boilers or industrial
furnaces operated under the interim status standards of
35 Ill. Adm. Code 726.203 shall either prepare and
submit a trial burn plan and perform a trial burn in
accordance with the requirements of the Section or
submit
other
information
as
specified
in
Section
703.208 (a) (6).
A~~licantswho submit a trial burn olan
and receive approval before submission of the part B
permit apnlication shall complete the trial burn and
submit the results specified in subsection
(f) with the
part_B_permit application.
If completion of this
process conflicf~,swith the date set for submission of
the part B application, the applicant shall contact the
Agency to establish a later date for submission of the
part B application or the trial burn results.
If the
applicant submits a trial burn plan with part B of the
permit application, the trial burn must be conducted
and the results submitted within a time period prior to
permit issuance to be specified by the Agency.
(Source:
Added
at
16
Ill.
Reg.
,
effective
SUBPART
G:
CHANGES
TO
PERMITS
128—496
27
Section
703.280
Permit
Modification
at
the
Request
of
the
Permittee
a)
Class
1 modifications.
See Section 703.281.
b)
Class
2 modifications.
See Section 703.282.
c)
Class
3 modifications.
See Section 703.283.
d),
Other modifications.
1)
In
the
case
of
modifications
not
explicitly
listed
in Appendix A, the permittee
may
submit
a
Class
3
modification request to the Agency, or the
permittee may request a determination by the
Agency
that
the
modification
be
reviewed and
approved
as
a
Class
1
or
Class
2
modification.
If
the
permittee
requests
that
the
modification
be
classified
as
a Class
1 or 2 modification, the
permittee shall provide the Agency with the
necessary information to support the requested
classification.
2)
The
Agency
shall
make
the
determination
described
in
subsection
(d) (1)
a
promptly
as
practicable.
In
determining
the appropriate class for a
specific
modification,
the Agency shall consider
the
similarity
of
the
modification
to
other
modifications
codified
in
Appendix
A
and
the
following
criteria:
A)
Class
1 modification apply to minor changes
that keep the permit current with routine
changes
to
the
facility
or
its
operation.
These
changes
do
not
substantially
alter
the
permit
conditions
or
reduce
the
capacity
of
the
facility
to
protect
human
health
or
the
environment.
In the case of Class
1
modifications, the Agency may require prior
approval.
B)
Class
2 modifications apply to changes that
are
necessary
to
enable
a
permittee
to
respond,
in
a
timely manner, to
i)
Common variations
in
the types and
quantities of the wastes managed under
the
facility
permit,
ii)
Technological
advances,
and
iii) Changes necessary to comply with new
128—49
7
28
regulations,
where
these
changes
can
be
implemented without substantially
changing.
design
specifications
or
management
practices
in
the
permit.
C)
Class
3 modifications substantially alter the
facility or its operation.
e)
Temporary authorizations.
1)
Upon request of the permittee,
the Agency shall,
without prior public notice and comment, grant the
permittee
a
temporary
authorization
in
accordance
with this subsection.
Temporary authorizations
have
a
term
of
not
more
than
180
days.
2)
Procedures.
A)
The permittee may request a temporary
authorization for:
i)
Any Class
2 modification meeting the
criteria in subsection
(e) (3) (B), and
ii)
Any
Class
3
modification
that
meets
the
criteria
in
subsection
(e)
(3)
(B) (i);
or
that
meets
the
criteria
in
subsection
(e) (3) (B) (iii)
through
(v) and provides
improved management or treatment of a
hazardous waste already listed in the
facility permit.
B)
The temporary authorization request must
include:
i)
A
description
of
the
activities
to
be
conducted under the temporary
authorization;
ii)
An explanation of why the temporary
authorization
is
necessary;
and
iii) Sufficient information to ensure
compliance with 35 Ill. Ads. Code 724
standards.
C)
The permittee shall send a notice about the
temporary authorization request to all
persons
on
the
facility
mailing
list
maintained by the Agency and to appropriate
units
of
State
and
local
governments
as
specified
in
35
Ill.
Adm.
Code
705.163(a)
(5).
128—498
29
This
notification
must
be
made
within
seven
days
after
submission
of
the
authorization
request.
3)
The Agency shall approve or deny the temporary
authorization as quickly as practical.
To issue a
temporary authorization, the Agency shall find:
A)
The authorized activities are in compliance
with the standards of 35 Ill. Adm. Code.724.
B)
The
temporary
authorization
is
necessary
to
achieve
one
of
the
following
objectives
before
action
is
likely
to
be taken on a
modification
request:
1)
To
facilitate
timely
implementation
of
closure or corrective action activities;
ii)
To allow treatment or storage in tanks
or containers of restricted wastes in
accordance
with
35
Ill. Adni.Code 728;
iii)
To
prevent
disruption
of
ongoing
waste
management
activities;
iv)
To
enable
the
permittee
to
respond
to
sudden
changes
in the types or
quantities
of
the
wastes
managed
under
the facility permit; or
v)
To facilitate other changes to protect
human
health
and
the
environment.
4)
A temporary authorization shall be reissued for
one
additional
term
of
up
to
180 days provided
that the permittee has requested a Class
2 or
3
permit
modification
for
the activity covered in
the
temporary
authorization,
and:
A)
The reissued temporary authorization
constitutes
the
Agency’s decision on a Class
2 permit modification in accordance with
Section 703.282(f)(l)(D)
or (f)(2)(D),
or
B)
The Agency determines that the reissued
temporary authorization involving a Class
3
permit modification request is warranted to
allow the authorized activities to continue
while the modification procedures of 35 Ill.
Adm.
Code
703.283
are
conducted.
128—499
30
f)
Public notice and appeals of permit modification
decisions.
1)
The Agency shall notify persons on the facility
mailing list and appropriate units of State and
local government within 10 days of any decision to
grant or deny a Class
2 or
3 permit modification
request.
The Agency shall also notify such
persons within 10 days after an automatic
authorization for a Class
2 modification goes into
effect under Section 703.282(f) (3)
or (f)(5).
2)
The Agency’s decision to grant or deny a Class
2
or
3 permit modification request may be appealed
under the permit appeal procedures of 35 Ill.
Adm.
Code
705.212.
3)
An
automatic authorization that goes into effect
under Section 703.282(f) (3)
or
(f)
(5)
may
be
appealed under the permit appeal procedures of 35
Ill.
Ads. Code 705.212; however, the permittee may
continue
to conduct the activities pursuant to the
automatic
authorization
until
the Board enters a
final order on the appeal notwithstanding the
provisions
of
35
Ill.
Adm.
Code
705.204.
g)
Newly listed or iacntiziea wastesregulated wastes and
units.
1)
The permittee is authorized to continue to manage
wastes listed or identified as hazardous under
35
Ill. Ads. Code 721 if the
permittee.
or
to
continue to manage hazardous waste in units newly
regulated as hazardous waste management units,
if:
A)
WasThe unit was in existence as a hazardous
waste facility with respect to the newly
listed or characterized waste or newly
regulated waste management unit on the
effective date of the final rule listing or
identifying
the
waste,
or
requlating
the
unit
B)
Cubmit3The permittee submits a Class
1
modification request on or before the date on
which
the
waste
becomes
subject
to
the
new
requirements;
C)
~sThe permittee is in compliance with the
applicable standards of 35 Ill.
Adm. Code 725
and 726
128—500
31
D)
In
tne
case oz
~Ihe permittee also submits a complete permit
class
2 or
3 modification request within 180
days after
the
effective
date
of
the
rule
listing or identifying the waste,
or
sub-iecting the unit to management standards
under 35 Ill. Ads. Code 724.
725
or
726
and
E)
In
the
case
of
land disposal units,
~Jj~
permittee
certifies
that
such
unit
is
in
compliance with all applicable requirements
Qf.
35 Iii. Ads. Code 725
,f~
groundwater
monitoring and financial responsibility
requirements on the date 12 months after the
effective
date
of
the
rule
identifying
or
listing
the
waste
as
hazardous,
or
regulating
the
unit
as
a
hazardous
waste
management
unit.
If
the
owner
or
operator fails to
clurifycertify
compliance
with
~jJ.
these
requirements,
the
owner
or
operator
loses
authority
to
operate under this Section.
2)
New
wastes
or
units
added
to
a
facility’s
permit
under this subsection do not constitute expansions
for the~purposeof the 25 percent capacity
expansion limit for Class
2 modifications.
h)
Permit modification list.
The Agency shall maintain a
list
of
all
approved
permit
modifications
and
shall
publish a notice once a year in a State—wide newspaper
that an updated list is available for review.
-f’Board
Note:
Derived
from
40 CFR 270.42(d) through
(h),
as
amended
at
53
Fed.
Reg.
37934,
Septcmbcr
20,
1988.)(1990), as amended at 56 Fed. Req.
7206.
February
21,
1991,
and at 56 Fed. Reg.
32688, July 17,
1991.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section 703.283
Class. 3 Modifications
a)
For Class
3 modifications,
listed in Appendix A, the
permittee shall submit a modification request to the
Agency which:
1)
Describes
the
exact
change
to
be
made
to
the
permit
conditions
and
supporting
documents
referenced
by
the
permit;
2)
Identifies that the modification is a Class
3
modification;
128—50
1
32
3)
Explains
why
the
modification
is
needed;
and
4)
Provides the applicable information required by
Section 703.181 through 703.105703.187, 703.201
through 703.207703.209, 703.221 through 703.225~.
and 703.230 and 703.232.
b)
The permittee shall send a notice of the modification
request to all persons on the facility mailing list
maintained
by
the
Agency
and’to the appropriate units
of State and local government as specified in 35 Iii.
Ads. Code 705.163(a) (5) and shall publish this notice
in
a
newspaper
of
general circulation in the county in
which the facility is located.
This notice must be
mailed and published within
7 days before or after the
date
of
submission
of
the modification request, and the
permittee shall provide to the Agency evidence of the
mailing and publication.
The notice must include:
1)
Announcement of a 60—day comment period,
in
accordance with subsection
(e), and the name and
address of an Agency contact to whom comments must
be sent;
2)
Announcement of the date, time and place for a
public
meeting
held
in
accordance
with
subsection
(d);
3)
Name
and
telephone
number
of
the
permittee’s
contact person;
4)
Name
and
telephone
number
of
an Agency contact
person;
5)
Locations where copies of the modification request
and any supporting documents can be viewed and
copied; and
6)
The
following
statement:
“The
perinittee’s
compliance history during the life of the permit
being modified is available from the Agency
contact person.”
C)
The permittee shall place a copy of the permit
modification
request
and
supporting
documents
in
a
location
accessible
to
the
public
in
the
vicinity
of
the permitted facility.
d)
The
permittee
shall
hold
a
public
meeting
no
earlier
than 15 days after the publication of the notice
required in subsection
(b) and no later than 15
days
128—502
33
before the close of the 60-day comment period.
The
meeting must be held to the extent practicable in the
vicinity of the permitted facility.
e)
the public shall be provided 60 days to comment on the
modification
request.
The
comment
period
will
begin
on
the date the permittee publishes the notice in the
local newspaper.
Comments must be submitted to the
Agency contact identified in the public notice.
f)
After the cOnclusion of the 60-day comment period, the
Agency shall grant or deny the permit modification
request according to the permit modification procedures
of 35 Ill. Ads. Code 705.
In addition, the Agency
shall consider and respond to all significant written
comments received during the 60—day comment period.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section
703.Appendix
A
Classification
of
Permit
Modifications
Class
Modifications
A.
General
Permit
Provisions
1
1.
Administrative and informational changes.
1
2.
Correction of typographical errors.
1
3.
Equipment replacement or upgrading with
functionally equivalent components
(e.g., pipes,
valves, pumps, conveyors,
controls).
4.
Changes in the frequency of or procedures for
monitoring, reporting,
sampling or maintenance
activities by the permittee:
1
a.
To provide for more frequent monitoring,
reporting or maintenance.
2
b.
Other
changes.
5.
Schedule of compliance:
1*
a.
Changes in interim compliance dates, with
prior approval of the Agency.
BOARD
NOTE:
~*1
indicates that prior Agency
approval, is required.
3
b.
Extension of final compliance date.
128—503
34
1*
6.
Changes in expiration date of permit to allow
earlier permit termination, with prior approval of
the Agency.
1*
7.
Changes in ownership or operational control of a
facility, provided the procedures of Section
703.260(b)
are followed.
B.
General Facility Standards
1.
Changes to waste sampling or analysis methods:
1
a.
To conform with Agency guidance or Board
regulations.
1
b.
To incorporate changes associated with F039
(multi—source
leachate)
sampling
or
analysis
methods.
2
c.
Other changes.
2.
Changes to analytical quality assurance/control
plan:
1
a.
To conform with agency guidance or
regulations.
2
b.
Other
changes.
1
3.
Changes
in
procedures for maintaining the
operating record.
2
4.
Changes in frequency or content of inspection
schedules.
5.
Changes in the training plan:
2
a.
That affect the type or decrease the amount
of training given to employees.
1
b.
Other changes.
6.
Contingency plan:
2
a.
Changes
in
emergency
procedures
.,
spill
or release response procedures).
1
b.
Replacement
with
functionally
equivalent
equipment,
upgrade or relocate emergency
equipment listed.
128—504
35
2
c.
Removal
of
equipment
from
emergency
equipment
list.
d.
Changes
in
name,
address
or phone number of
coordinators or other persons or agencies
identified in the plan.
Note:
When a permit modification (such as
introduction of
a
new unit)
requires a change
in facility plans or other general facility
standards,
that change must be reviewed under
the same procedures as the permit
modification.
C.
Groundwater Protection
1.
Changes
to
wells:
2
a.
Changes in the number,
location, depth or
design of upgradient or downgradient wells of
permitted groundwater monitoring system.
b.
Replacement of an existing well that has been
damaged or rendered inoperable,
without
change to location, design or depth of the
well.
1*
2.
Changes
in
groundwater
sampling
or
analysis
procedures
or
monitoring
schedule,
with
prior
approval of the Agency.
1*
3.
Changes in statistical procedure for determining
whether a statistically significant change in
groundwater quality between upgradient and
downgradient wells has occurred, with prior
approval of the Agency.
2*
4.
Changes in point of compliance.
5.
Changes in indicator parameters,
hazardous
constituents or concentration limits
(including
ACL5 (Alternate Concentration Limits)):
3
a.
As specified in the groundwater protection
standard.
2
b.
As specified in the detection monitoring
program.
2
6.
Changes to a detection monitoring program as
required by 35 Ill.
Ads. Code 724.198(j), unless
otherwise specified in this Appendix.
128—505
36
7.
Compliance monitoring program:
3
a.
Addition of compliance monitoring program as
required by 35 Ill. Ads. Code 724.198(h) (4)
and 724199.
2
b.
Changes to a compliance monitoring program as
required by 35 Ill.
Ads. Code 724.199(k),
unless
otherwise
specified
in
this
Appendix.
8.
Corrective action program:
3
a.
Addition of a corrective action program as
required by 35 Ill. Adm. Code 724.199(i) (2)
and 724.200.
2
b.
Changes to a corrective action program as
required by 35 Ill. Adm. Code 724.200(h),
unless otherwise specified in this Appendix.
D.
Closure
1.
Changes to the closure plan:
1*
a.
Changes in estimate of maximum extent of
operations or maximum inventory of waste on—
site at any time during the active life of
the facility, with prior approval of the
Agency.
1*
b.
Changes in the, closure schedule for any unit,
changes in the. final closure schedule for the
facility or extension of the closure period,
with prior approval of the Agency.
1*
c.
Changes in the expected year of final
closure, where other permit conditions are
not changed, with prior approval of the
Agency.
1*
d.
Changes in procedures for decontamination of
facility equipment or structures, with prior
approval of the Agency.
2
e.
Changes in approved closure plan resulting
from
unexpected
events
occurring
during
partial or final closure, unless otherwise
specified in this Appendix.
2
f.
Extension of the closure period to allow a
landfill, surface impoundment or land
128—506
37
treatment unit to receive non—hazardous
wastes after final receipt of hazardous
wastes under 35 Ill. Ads. Code 724.213(d)
or
(e).
3
2.
Creation of a new landfill unit as part of
closure.
3.
Addition of the following new units to be used
temporarily for closure activities:
3
a.
Surface ixnpoundsents.
3
b.
Incinerators.
3
c.
Waste piles that do not comply with 35 Ill.
Adm.
Code
724.350(c).
2
d.
Waste piles that comply with 35 Ill. Adm.
Code 724.350(c).
2
e.
Tanks
or
containers
(other
than
specified
below).
1*
f.
Tanks used for neutralization, dewatering,
phase
separation
or
component
separation,
with prior approval of the Agency.
E.
Post—Closure
1
1.
Changes
in
name,
address
or
phone
number
of
contact
in
post—closure
plan.
2
2.
Extension of post-closure care period.
3
3.
Reduction in the post—closure care period.
1
4.
Changes to the expected year of final closure,
where other permit conditions are not changed.
2
5.
Changes
in. post-closure plan necessitated by
events occurring during the active life of the
facility, including partial and final Olosure.
F.
Containers
1.
Modification
or
addition
of
container
units:
3
a.
Resulting in greater than 25
increase in the
facility’s container storage capacity, except
as
provided
in
F(l)
(c)
and
F(4)
(a).
128—
507
38
2
b.
Resulting in up to 25
increase in the
facility’s container storage capacity, except
as
provided
in
F(1)
(C)
and F(4) (a).
c.
Or
treatment
processes
necessary
to
treat
wastes that are restricted from land disposal
to meet some or all of the applicable
treatment
standards
or
to
treat wastes to
satisfy (in whole or in part)
the standard of
“use
of
practically
available
technology
that
yields
the
greatest
environmental
benefit”
contained in 40 CFR 268.8(a) (2) (ii),
incorporated by reference in 35 Ill. Adm.
Code 728.108, with prior approval of the
Agency.
This modification may also involve
the addition of new waste codes or narrative
description of wastes.
It is not applicable
to dioxin-containing wastes
(F020,
F021,
F022,
F023,
F026,
F027 and F028).
2.
2
a.
Modification of a container unit without
increasing the capacity of the unit.
b.
Addition
of
a
roof
to
a
container
unit
without alteration of the containment’ system.
3.
Storage of different wastes in containers,
except
as
provided
in
F(4):
3
a.
That require additional or different
management practices from those authorized in
the permit.
2
b.
That
do
not
require
additional
or
different
management practices from those authorized in
the permit.
Note:
See Section .703.280(g)
for
modification procedures to be used for~the
management of newly listed or identified
wastes.
4.
Storage or treatment of different wastes in
containers:
2
a.
That require addition of units or change in
treatment process or management standards,
provided that the wastes are restricted from
land disposal and are to be treated to meet
some or all of the applicable treatment
128—508
39
standards, or are to be treated to satisfy
(in whole or in part) the standard of “use of
practically available technology that yields
the greatest environmental benefit” contained
in
40’ CFR 268.8(a) (2) (ii),
incorporated by
reference in 35 Ill. Ads. Code 728.108.
It
is not applicable to dioxin—containing wastes
(F020,
F021,
F022,
F023, F026,
F027 and
F028).
b.
That do not require the addition of units or
a change in the treatment process or
management standards, and provided that the
units have previously received wastes of the
same type
(e.g.,
incinerator scrubber water).
This
modification
is
not
applicable
to
dioxin-containing
wastes
(F020,
F021,
F022,
F023, F026, F027 and F028)
G.
Tanks
1.
3
a.
Modification
or
addition
of
tank
units
resulting
in
greater
than
25
increase
in
the
facility’s tank capacity, except as provided
in
paragraphs
G(l)
(c),
G(1) (d)
and
G(1)
(e).
2
b.
Modification or addition of tank units
resulting in up. to 25
increase in the
facility’s tank capacity, except as provided
in
paragraphs
G(l)
(d)
and
G(1) (e).
2
c.
Addition of a new tank that will operate for
more than 90 days using any of the following
physical
or
chemical
treatment
technologies:
neutralization, dewatering, phase separation
or component separation.
1*
d.
After prior approval of the Agency, addition
of a new tank that will operate for up to 90
days using any of the following physical or
chemical treatment technologies:
neutralization, dewatering, phase separation
or component separation.
a.
e.
Modification or addition of tank units or
treatment processes that are necessary to
treat wastes that are restricted from land
disposal to meet some or all of the
applicable treatment standards or to treat
wastes
to
satisfy
(in
whole
or
in
part)
the
128—509
40
standard of “use of practically available
technology that yields the greatest
environmental, benefit” contained in 40 CFR
268.8(a) (2) (ii),
incorporated by reference in
35
Ill. Ads. Code 728.108, with prior
approval of the Agency.
This modification
may also involve the addition of new waste
codes.
It is ‘not applicable to dioxin—
containing wastes
(F020,
F021,
F022,
F023,
F026,
F027 and F028).
2
2.
Modification of a tank unit or secondary
containment system without increasing the capacity
of the unit.
3.
Replacement of a tank with a tank that meets the
same design standards and has a capacity within
+1-
10
of the replaced ‘tank provided:
a.
The capacity difference is no more than 1500
gallons,
b.
The facility’s permitted tank capacity is not
increased and
c.
The replacement tank meets the same
conditions
in
the
permit.
2
4.
Modification of a tank management practice.
5.
Management of different wastes in tanks:
3
a.
That require additional or different
management practices,
tank design, different
fire protection specifications or
significantly different tank treatment
process from that authorized in the permit,
except as provided in paragraph G(5) (c).
2
b.
That do not require additional or different
management practices,
tank design, different
fire protection specification or
significantly different tank treatment
process than authorized in the permit,
except
as provided in paragraph G(5) (d).
Note:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
c.
That require addition of units or change in
128—510
42.
treatment processes or management standards,
provided that the wastes are restricted from
land disposal and are to be treated to meet
some or all of the applicable treatment
standards, or that are to be treated to
satisfy (in whole or in part)
the standard of
“use of practically available technology that
yields the greatest environmental benefit”
contained in 40 CFR 268.8(a) (2) (ii),
incorporated by reference in 35 Ill. Ads.
Code 728.108.
The modification is not
applicable to dioxin—containing wastes (F020,
F02l, F022,
F023, F026,
F027 and F028).
d.
That do not require the addition of units or
a change in the treatment process or
management standards, and provided that the
units have previously received wastes of the
same type (e.g.,
incinerator scrubber water).
This modification is not applicable to
dioxin-containing wastes
(F020, F021,
F022,
F023, F026,
F027 and F028).
H.
Surface Impoundments
3
1.
Modification or addition of surface impoundment
units that result in increasing the facility’s
surface impoundment storage or treatment capacity.
3
2.
Replacement of a surface impoundsent unit.
2
3.
Modification of a surface impoundment unit without
increasing the facility’s surface impoundment
storage or treatment capacity and without
modifying the unit’s liner,
leak detection system
or leachate collection system.
2
4.
Modification of a surface impoundment management
practice.
5.
Treatment, storage or disposal of different wastes
in surface impoundments:
3
a.
That require additional or different
management practices or different design of
the liner or leak detection system than
authorized in the permit.
2
b.
That do not’ require additional or different
management practices or different design of
the liner or leak detection system than
authorized in the permit.
128—5
11
42
Note:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
c.
That
are
wastes
restricted
from
land
disposal
that meet the applicable treatment standards
or that are treated to satisfy the standard
of “use of practically available technology
that yields the greatest environmental
benefit” contained in 40 CFR 268.8(a) (2) (ii),
incorporated by reference in 35 Ill. Adm.
Code 728.108, and provided that the unit
meets the minimum technological requirements
stated
in
40
CFR
268.5(h)
(2),
incorporated
by
reference in 35
Ill.
Adm. Code 728.105.
This
modification is not applicable to dioxin-
containing wastes
(F020, F02l,
F022,
F023,
F026, F027 and F028).
d.
That are residues from wastewater treatment
or incineration, provided the disposal occurs
in a unit that meets the minimum
technological requirements stated in 40 CFR
268.5(h) (2), incorporated by reference in 35
Ill.
Adm. Code 728.105,
and provided further
that the surface impoundment has previously
received wastes of the same type (for
example,
incinerator
scrubber
water).
This
modification is not applicable to dioxin-
containing wastes
(F020, F021, F022,
F023,
F026,
F027
and’ F028).
I.
Enclosed Waste Piles.
For all waste piles,
except
those complying with 35 Ill. Adm. Code 724.350(c),
modifications are treated the same as for a landfill.
The following modifications are applicable only to
waste piles complying with 35 Ill. Adm. Code
724.350(c)
1.
Modification or addition of waste pile units:
3
a.
Resulting
in
greater
than
25
increase
in
the
facility’s waste pile storage or treatment
capacity.
2
b.
Resulting in up to 25
increase in the
facility’s waste pile storage or treatment
capacity.
2
2.
Modification of waste pile unit without increasing
128—5
12
43
the capacity of the unit.
1
3.
Replacement of a waste pile unit with another
waste pile unit of the same design and capacity
and meeting all waste pile conditions in the
permit.
2
4.
Modification
of
a
waste
pile
management
practice.
5.
Storage or treatment of different wastes in waste
piles:
3
a.
That require additional or different
management practices or different design of
the unit.
2
b.
That do not require additional or different
management practices or different design of
the
unit.
Note:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
J.
Landfills and Unenclosed Waste Piles
3
1.
Modification
or
addition
of
landfill
units
that
result
in
increasing
the
facility’s
disposal
capacity.
3
2.
Replacement
of
a
landfill.
3
3.
Addition
or
modification
of
a
liner,
leachate
collection system, leachate detection system, run-
off
control
or
final
cover
system.
2
4.
Modification of a landfill unit without changing a
liner,
leachate collection system, leachate
detection system, run-off control or final cover
system.
2
5.
Modification of a landfill management practice.
6.
Landfill different wastes:
3
a.
That require additional or different
management practices, different design of the
liner,
leachate collection system or leachate
detection system.
2
b.
That do not require additional or different
128—513
44
management practices, different design of the
liner,
leachate collection system or leachate
detection system.
Note:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
c.
That are wastes restricted from land disposal
that meet the applicable treatment standards
or that are treated to satisfy the standard
of “use of practically available technology
that yields the greatest environmental
benefit” contained in 40 CFR 268.8(a) (2) (ii),
incorporated by reference in 35
Ill. Ads.
Code 728.108, and provided that the landfill
unit meets the minimum technological
regulrements stated in 40 CFR 268.5(h) (2),
incorporated by reference in 35 Ill. Adm.
Code 728.105.
This modification is not
applicable to dioxin-containing wastes
(F020,
F021,
F022, F023,
F026,
F027 and F028).
d.
That are residues from wastewater treatment
or incineration, provided the disposal occurs
in a landfill unit that meets the minimum
technological reguirements stated in 40 CFR
268.5(h) (2), incorporated by reference in 35
Ill. Adm. Code 728.105, and provided further
that the landfill has previously received
wastes of the same type (for example,
incinerator ash).
This modification is not
applicable to dioxin-containing wastes
(F020,
F021,
F022, F023,
F026,
F027 and F028).
K.
Land
Treatment
3
1.
Lateral expansion of or other modification of
a
land treatment unit to increase area extent.
2
2.
Modification of run-on control system.
3
3.
Modify run-off control, system.
2
4.
Other modification of land treatment unit
component specifications or standards required in
permit.
5.
Management of different wastes in land treatment
units:
128—5 14
45
3
a.
That require a change in permit operating
conditions or unit design specifications.
2
b.
That do .not require a change.in permit
operating conditions or unit design
specifications.
Note:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
6.
Modification of a land treatment unit management
practice to:
3
a.
Increase rate or change method of waste
application.
b.
Decrease rate of waste application.
2
7.
Modification of a land treatment unit management
practice to change measures of pH or moisture
content or to enhance microbial or chemical
reactions.
3
8.
Modification
of
a
land
treatment
unit
management
practice to grow food chain crops, to add to or
replace existing permitted crops with different
food chain crops or to modify operating plans for
distribution of animal feeds resulting from such
crops.
3
9.
Modification
of
operating
practice
due
to
detection
of
releases
from
the
land
treatment
unit
pursuant to 35 Ill. Ads. Code 724.378(g) (2).
3
10.
Changes in the unsaturated zone monitoring system
resulting in a change to the location, depth,
number of sampling points or replace unsaturated
zone monitoring devices or components of devices
with devices or components that have
specifications different from permit requirements.
2
11.
Changes in the unsaturated zone monitoring system
that do not result in a change to the location,
depth, number of sampling points,’ or that replace
unsaturated zone monitoring devices or components
of devices with devices or components having
specifications different from permit requirements.
2
12.
Changes in background values for hazardous
constituents in soil and soil-pore liquid.
128—5 15
46
2
13.
Changes in sampling, analysis or statistical
procedure.
2
14.
Changes in land treatment demonstration program
prior to or during the demonstration.
1*
15.
Changes in any condition specified in the permit
for a land treatment unit to reflect results of
the land treatment demonstration, provided
performance standards are met, and the Agency’s
prior approval has been received.
1*
16.
Changes to allow a second land treatment
demonstration to be conducted when the results of
the first demonstration have not shown the
conditions under which the wastes can be treated
completely, provided the conditions for the second
demonstration are substantially the same as the
conditions for the first demonstration and have
received the prior approval of the Agency.
3
17.
Changes to allow a second land treatment
demonstration
to
be conducted when the results of
the first demonstration have not shown the
conditions under which the wastes can be treated
completely, where the conditions for the second
demonstration are not substantially the same as
the conditions for the first demonstration.
2
18.
Changes in vegetative cover requirements for
closure.
L.
Incinerators, Boilers and Industrial Furnaces
3
1.
Changes to increase by more than 25
any of the
following limits authorized in the permit: A
thermal feed rate limit,
a waste fced rate limit
or an organic chlorine feed rate limita feedstream
feed rate limit,
a chlorine/chloride feed rate
limit,
a metal feed rate limit or an ash feed rate
limit.
The Agency shall require a new trial burn
to substantiate compliance with the regulatory
performance standards unless this demonstration
can be made through other means.
2
2.
Changes to increase by up to 25
any of the
following limits authorized in the permit:
A
thermal feed rate limit,
a waste fced limit or an
organic chlorine fccd rate limita feedstream feed
rate limit,
a chlorine/chloride feed rate limit,
a
metal feed rate limit or an ash feed rate limit.
128—5 16
47
The Agency shall require a new trial burn to
substantiate compliance with the regulatory
performance standards unless this demonstration
can be made through other means.
3
3.
Modification of an incinerator, boiler or
industrial furnace unit by changing the internal
size or geometry of the primary or secondary
combustion units, by adding
a primary or secondary
combustion unit, by substantially changing the
design of any component used to remove HClLQj~2~
metals or particulatee from the combustion gases
or by changing other features of the incinerator~
boiler or industrial furnace that could affect its
capability to meet the regulatory performance
standards.
The Agency shall require a new trial
burn
to
substantiate
compliance
with
the
regulatory performance standards,
unless this
demonstration can be made through other means.
2
4.
Modification
of
an
incinerator,
boiler
or
industrial furnace unit in a manner that will not
likely
affect
the
capability
of
the
unit
to
meet
the
regulatory
performance
standards
but
which
will
change
the
operating
conditions
or
monitoring
requirements
specified
in
the
permit.
The
Agency
may
require
a
new
trial
burn
to
demonstrate
compliance
with
the
regulatory
performance
standards.
5.
Operating
requirements:
3
a.
Modification
of
the
limits
specified
in
the
permit for minimum or maximum combustion gas
temperature,
minimum
combustion
gas
residence
time~
e~
oxygen
concentration
in
the
secondary combustion chamber,
flue gas carbon
monoxide or hydrocarbon concentration.
maximum
temperature
at
the
inlet
to
the
PM
emission control system or operating
parameters
for
the air pollution control
system.
The Agency shall require a new trial
burn to substantiate compliance with the
regulatory performance standards unless this
demonstration can be made through other
means.
3
b.
Modification of any stack gas emission limits
specified in the permit,
or modification of
any conditions in the permit concerning
emergency shutdown or automatic waste feed
cutoff procedures or controls.
128—517
48
2
c.
Modification
of
any
other
operating
condition
or
any
inspection
or
recordkeeping
requirement
specified
in
the
permit.
6.
incineration ofBurnjng different wastes:
3
a.
If the waste contains a POHC that is more
difficult to incinerateburn than authorized
by the permit or if incinerationburning of
the waste requires compliance with different
regulatory
performance
standards
than
specified
in
the
permit,
the
Agency
shall
require a new trial burn to substantiate
compliance
with
the
regulatory
performance
standards, unless this demonstration can be
made through other means.
2
b.
If
the waste does not contain a POHC that is
more
difficult
to
incinerateburn
than
authorized by the permit and if
incinerationburning
of
the waste does not
require compliance with different regulatory
performance
standards
than
specified
in
the
permit.
BOARD
NOTE:
See Section 703.280(g)
for
modification procedures to be used for the
management of newly listed or identified
wastes.
7.
Shakedown and trial, burn:
2
a.
Modification
of’
the
trial burn plan or any of
the
permit
conditions
applicable
during
the
shakedown period for determining’ operational
readiness
after
construction,
the
trial
burn
period or the period immediately following
the trial burn.
1*
b.
Authorization of up to an additional 720
hours of waste incinerationburning during the
shakedown
period
for
determining
operational
readiness after construction, with the prior
approval
of
the
Agency.
1*
c.
Changes
in
the
operating
requirements
set
in
the permit for conducting a trial burn,
provided the change is minor and has received
the prior approval of the Agency.
1*
d.
Changes in the ranges of the operating
128—518
49
requirements set in the permit to reflect the
results of the trial burn, provided the
change is minor and has received the prior
approval of the Agency.
8.
Substitution of an alternate type of nonhazardous
waste fuel that is not specified in the permit.
BOARD
NOTE:
Derived from 40 CFR 270.42, Appendix
I
(1990), as amended at 56 Fed. Req.
7206,
February 21,
1991.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
128—519
50
TITLE 35~ ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER I:
POLLUTION
CONTROL
BOARD
SUBCHAPTER
C:
HAZARDOUS
WASTE OPERATING REQUIREMENTS
PART
720
HAZARDOUS
WASTE
MANAGEMENT SYSTEM:
GENERAL
SUBPART A:
GENERAL
PROVISIONS
Section
720.101
Purpose,
Scope
and
Applicability
720.102
Availability
of
Information;
Confidentiality
of
Information
720.103
Use of Number and Gender
SUBPART
B:
DEFINITIONS
Section
720.110
720. 111
SUBPART
C:
RULEMAKING
PETITIONS
AND
OTHER
PROCEDURES
Section
Rulemaking
Alternative Equivalent Testing Methods
Waste Delisting
Procedures for Solid Waste Determinations
Solid Waste Determinations
Boiler Determinations
Procedures for Determinations
Additional regulation of certain hazardous waste
Recycling Activities on a case—by—case Basis
720.141
Procedures for case—by-case regulation of hazardous
waste Recycling Activities
Appendix A
Overview of 40 CFR, Subtitle C Regulations
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27
of
the
Environmental
Protection
Act
(Ill.
Rev.
Stat.
1989,
ch.
111½, pars.
1022.4 and 1027).
SOURCE:
Adopted in R81—22,
43 PCB 427, at 5
Ill. Reg. 9781,
effective as noted in 35 Ill. Adm. Code 700.106; amended ~nd
codified in R81—22,
45 PCB 317, at 6 Ill. Reg.
4828, effective as
noted in 35
Ill. Ads.
Code 700.106; amended in R82-l9 at 7
Ill.
Reg.
14015, effective Oct.
12,
1983; amended in R84—9,
53 PCB 131
at
9
Ill. Reg.
11819, effective July 24,
1985; amended in R85-22
at 10
Ill. Reg.
968, effective January 2,
1986; amended in R86-l
at
10 Ill. Reg.
13998, effective August 12,
1986; amended in R86-
19 at 10 Ill.
Reg.
20630, effective December 2,
1986; amended in
R86—28 at 11 Ill. Reg.
6017, effective March 24,
1987; amended in
R86—46 at 11 Ill.
Req. 13435, effective August
4,
1987;
amended
in R87—5 at 11 Ill. Reg.
19280, effective November 12,
1987;
Definitions
References
720. 120
720.121
720. 122
720. 130
720. 131
720.132
720.133
720.140
128—520
51
amended in R87—26 at 12 Ill. Reg.
2450, effective January 15,
1988; amended in R87-39 at 12
Ill. Reg.
12999, effective July 29,
1988;
amended in R88-16 at 13 Ill.
Reg.
362, effective December
27,
1988; amended in R89—1 at
13 Ill. Reg.
18278,
effective
November 13,
1989; amended in R89—2 at 14 Ill. Reg.
3075,
effective February 20,
1990; amended in R89—9 at 14
Ill. Reg.
6225, effective April 16,
1990; amended in R90—10 at
14
Ill. Reg.
16450, effective September 25,
1990; amended in R90—17 at
15 Ill.
Reg.
7934, effective May 9,
1991; amended in R90-11 at 15 111.
Reg. 93~3,effective June 17,
1991; amended in R91-1 at 15 Ill.
Reg.
14446,
effective October
1,
1991;
amended in R91-l3 at 16
Ill. Reg.
,
effective
SUBPART
B:
DEFINITIONS
Section 720.110
Definitions
When used in 35 Ill. Ada. Code 720 through ~2-S~2~and 728 only,
the following terms have the meanings given below:
“Aboveground tank” means
a device meeting the
definition of “tank” that is situated in such a way
that the entire surface area of the tank is completely
above the plane of the adjacent surrounding surface and
the entire surface area of the tank (including the tank
bottom)
is able to be visually inspected.
“Act”
or “RCRA” means the Solid Waste Disposal Act,
as
amended by the Resource Conservation and Recovery Act
of 1976, as amended
(42 U.S.C.
6901 et seq.)
“Active life” of a facility means the period from the
initial receipt of hazardous waste at the facility
until the Agency receives certification of final
closure.
“Active portion” means that portion of a facility where
treatment,
storage or disposal operations are being or
have been conducted after May 19,
1980,
and which is
not a closed portion.
(See also “closed portion” and
“inactive portion”.)
“Administrator” means the.Adsinistrator of the U.S.
Environmental Protection Agency or the Administrator’s
designee.
“Agency” means the Illinois Environmental Protection
Agency.
“Ancillary equipment” means any device including,
but
not limited to,
such devices as piping, fittings,
flanges, valves and pumps, that is used to distribute,
128—521
52
meter or control the flow of hazardous waste from its
point of generation to storage or treatment tank(s),
between hazardous waste. storage and treatment tanks to
a point of disposal onsite, or to a point of shipment
for disposal off—site.
“Aquifer” means a geologic formation, group of
formations or part of a ~formationcapable of yielding a
significant amount of groundwater to wells or springs.
“Authorized representative” means the person
responsible for the overall operation of a facility or
an operational unit (i.e., part of a facility),
e.g.,
the plant manager, superintendent or person of
equivalent responsibility.
“Board” means the Illinois Pollution Control Board.
“Boiler” means an enclosed device using controlled
flame combustion and having the following
characteristics:
The unit must have physical provisions for
recovering and exporting thermal energy in the
form of’ steam, heated fluids or heated gases; and
the unit’s combustion chamber and primary energy
recovery section(s) must be of integral design.
To be of integral design, the combustion chamber
and the primary energy recovery s.ection(s)
(such
as waterwalls and superheaters) must be physically
formed into one manufactured or assembled unit.
A
unit in which the combustion chamber and the
primary energy recovery section(s)
are joined only
by ducts or connections carrying flue gas is not
integrally designed; however, secondary energy
recovery equipment (such as economizers or air
preheaters) need not be physically formed into the
same unit as the combustion chamber and the
primary energy recovery section.
The following
units are not precluded from being boilers solely
because they are not of integral design:
process
heaters
(units that transfer energy directly to a
process stream), and fluidized bed combustion
units; and
While in operation, the unit must maintain a
thermal energy recovery efficiency of at least 60
percent, calculated in terms of the recovered
energy compared with the thermal value of the
fuel; and
The unit must export and utilize at least 75
128—522
53
percent of the recovered energy, calculated on an
annual basis.
In this calculation, no credit
shall be given for recovered heat used internally
in the same unit.
(Examples of internal use are
the preheating of fuel or combustion air, and the
driving of induced or forced draft fans or
feedwater pumps); or
The unit is one which the Board has determined,
on
a case—by—case basis, to be a boiler, after
considering the standards in Section 720.132.
“Carbon regeneration unit” means any enclosed thermal
treatment device used to regenerate spent activated
carbon.
“Certification”
means
a
statement
of
professional
opinion based upon knowledge and belief.
“Closed Portion” means that portion of a facility which
an owner or operator has closed in accordance with the
approved facility closure plan and all applicable
closure requirements.
(See also “active portion” and
“inactive portion”.)
“Component” means either the tank or ancillary
equipment of a tank system.
“Confined aquifer” means an aquifer bounded above and
below by impermeable beds or by beds of distinctly
lower permeability than that of the aquifer itself; an
aquifer containing confined groundwater.
“Container” means any portable device in which a
material is stored,
transported, treated, disposed of
or otherwise handled.
“Contingency plan” means a document setting out an
organized, planned and coordinated course of action to
be followed in case of a fire, explosion or release of
hazardous waste or hazardous waste constituents which
could threaten human health or the environment.
“Corrosion expert” means a person who, by reason of
knowledge of the physical sciences and the principles
of engineering and mathematics., acquired by a
professional education and related practical
experience,
is qualified to engage in the practice of
corrosion control on buried or submerged metal piping
systems and metal tanks.
Such a person must be
certified as being qualified by the National
Association of Corrosion Engineers
(NACE)
or be a
128—523
54
registered professional engineer who has certification
or licensing that includes education and experience in
corrosion control on buried or submerged metal piping
systems and metal tanks.
“Designated facility”.
“Designated facility” means a hazardous waste
treatment, storage or disposal facility,
Which:
Has received a
RCRA permit
(or interim
status) pursuant to 35 Ill.
Ada. Code 702,
703 and 705;
Has received a
RCRA
permit from USEPA
pursuant to 40 CFR 124 and 270 (1989);
Has received a
RCRA
permit from a
state
authorized by USEPA pursuant to 40 CFR 271
(1989); or
Is regulated under 35 Ill. Ada. Code
721.106(c) (2)
or 266.Subpart F; and
Which has been designated on the manifest by the
generator pursuant to 35 Ill. Adm. Code 722.120.
If a waste is destined to a facility in a state,
other than Illinois, which has been authorized by
USEPA pursuant to 40 CFR 271, but which has not
yet obtained authorization to regulate that waste
as hazardous, then the designated facility must be
a facility allowed by the receiving state to
accept such waste.
“Dike” means an embankment or ridge of either natural
or manmade materials used to prevent the movement of
liquids, sludges, solids or other materials.
“Director” means the Director of the Illinois
Environmental Protection Agency.
“Discharge” or “hazardous waste discharge” means the
accidental or intentional spilling, leaking, pumping,
pouring, emitting, emptying or dumping of hazardous
waste into or on any land or water.
“Disposal” means the discharge, deposit,
injection,
dumping,
spilling, leaking or placing of any solid
waste or hazardous waste into or on any land or water
128—524
55
so that such solid waste or hazardous waste or any
constituent thereof may enter the environment or be
emitted into the air or discharged into any waters,
including groundwaters.
“Disposal facility” means a facility or part of a
facility at which hazardous waste is intentionally
placed into or on any land or water and at which waste
will remain after closure.
“Drip pad” means an engineered structure consisting of
a curbed, free—draining base, constructed of non—
earthen materials and designed to convey preservative
kick-back or drippage from treated wood, precipitation
and surface water run—on to an associated collection
system at wood preserving plants.
“Elementary
neutralization
unit”
means
a
device
which:
Is used for neutralizing wastes which are
hazardous only because they exhibit the
corrosivity characteristic defined in 35 Ill.
Ads.
Code 721.122 or are listed in 35
Ill.’ Adm. Code
721.Subpart D only for this reason; and
Meets the definition of tank, tank system,
container,
transport vehicle or vessel in this
Section.
“EPA” or “USEPA
“
means
United
States
Environmental
Protection Agency.
“EPA hazardous waste number” or “USEPA hazardous waste
number” means the
number
assigned by EPA to each
hazardous waste listed in 35 Ill. Ads. Code 721.Subpart
D and to each characteristic identified in 35 Ill.
Ada.
Code 721.Subpart C.
“EPA identification number” or “USEPA identification
number” means the number assigned by USEPA pursuant to
35 Ill.
Ads. Code 722 through 725 to each generator,
transporter and treatment,
storage or disposal
facility.
“EPA region” means the states and territories found in
any one of the following ten regions:
Region
I:
Maine, Vermont, New Hampshire,
Massachusetts,
Connecticut and Rhode Island
Region II:
New York, New Jersey, Commonwealth of
Puerto Rico and the U.S. Virgin Islands
128—525
56
Region III:
Pennsylvania, Delaware, Maryland,
West Virginia, Virginia and the District of
Columbia
Region IV:
Kentucky, Tennessee,
North Carolina,
Mississippi, Alabama, Georgia,
South Carolina and
Florida
Region V:
Minnesota, Wisconsin,
Illinois,
Michigan, Indiana and Ohio
Region VI:
New Mexico,
Oklahoma, Arkansas,
Louisiana and Texas
Region VII:
Nebraska, Kansas, Missouri and Iowa
Region VIII:
Montana, Wyoming, North Dakota,
South Dakota, Utah and Colorado
Region IX:
California, Nevada,
Arizona, Hawaii,
Guam, American Samoa and Commonwealth of the
Northern Mariana Islands
Region X:
Washington, Oregon,
Idaho and Alaska
“Equivalent method” means any testing or analytical
method approved by the Board pursuant to Section
720. 120.
“Existing hazardous waste management
(HWM)
facility” or
“existing facility” means a facility which was in
operation or for which construction commenced on or
before November
19,
1980.
A facility had commenced
construction if the
owner
or operator had obtained the
federal, state and local approvals or permits necessary
to begin physical construction and either
A continuous on—site, physical construction program had
begun or the owner or operator had entered into
contractual obligations
——
which could not be cancelled
or modified without substantial loss
-—
for physical
construction of the facility to be completed within a
reasonable time.”Existing portion” means that land
surface area of an existing waste management unit,
included in the original Part A permit application, on
which wastes have been placed prior to the issuance of
a permit.
“Existing tank system” or “existing component” means a
tank system or component that is used for the storage
or treatment of hazardous waste and that is in
128—526
57
operation,
or for which installation has commenced on
or prior to July 14, 1986.
Installation will be
considered to have commenced if the owner or operator
has obtained all federal, State and local approvals or
permits necessary to begin physical construction of the
site or installation of the tank system and if either
A continuous on—site physical construction or
installation program has begun; or
The owner or operator has entered into contractual
obligations
——
which cannot be canceled or
modified without substantial loss
-—
for physical
construction of the site or installation of the
tank system to be completed within a reasonable
time.
“Facility” means all contiguous land and structures,
other appurtenances and improvements on the land used
for treating, storing or disposing of hazardous waste.
A facility may consist of several treatment,
storage or
disposal operational units
(e.g., one or more
landfills, surface impoundments or combinations of
them).
“Final closure” means the closure of all hazardous
waste management units at the facility in accordance
with all applicable closure requirements so that
hazardous waste management activities under 35 Ill.
Ada. Code 724 and 725 are, no longer conducted at the
facility unless subject to the provisions of 35 Ill.
Adm. Code 722.134.
“Federal agency” means any department,
agency or other
instrumentality of the federal government,
any
independent agency or establishment of the federal
government including any government corporation and the
Government Printing Office.
“Federal, state and local approvals or permits
necessary to begin physical construction” means permits
and approvals required under federal, state or local
hazardous waste control statutes, regulations or
ordinances.
“Food—chain crops” means tobacco, crops grown for human
consumption
and
crops
grown
for
feed
for
animals
whose
products are consumed by humans.
“Freeboard” means the vertical distance between the top
of
a
tank
or
surface
impoundment
dike
and
the
surface
of
the
waste
contained
therein.
128—527
58
“Free liquids” means liquids which readily separate
from the solid portion of a waste under ambient
temperature and pressure.
“Generator” means any person, by site, whose act or
process produce hazardous waste identified or listed in
35 Ill. Ads. Code 721 or whose act first causes a
hazardous waste to become subject to regulation.
“Groundwater” means water below the land surface in a
zone of saturation.
“Hazardous waste” means a hazardous waste as defined in
35
Ill.
Ads.
Code
721.103.
“Hazardous waste constituent” means a constituent which
caused
the
hazardous
waste
to
be
listed
in
35
Ill.
Ada.
Code
721.Subpart
D,
or
a
constituent
listed
in
of
35
Ill.
Adm.
Code
721.124.
“Hazardous waste management unit”
is a contiguous area
of
land
on
or
in
which
hazardous
waste
is
placed,
or
the
largest
area
in
which
there
is
significant
likelihood of mixing hazardous waste constituents in
the same area.
Examples of hazardous waste management
units include a surface impoundment,
a waste pile,
a
land treatment area, a landfill cell,
an incinerator, a
tank and its associated p.iping and underlying
containment system and a container Storage area.
A
container
alone
does
not
constitute
a
unit;
the
unit
includes
containers
and
the
land
or
pad
upon
which
they
are placed.
“Inactive
portion”
means
that
portion
of
a
facility
which
is
not
operated
after
November
19,
1980.
(See
also “active portion” and “closed portion”.)
“Incinerator” means any enclosed device using
controlled flamc combustion which is neither a “boiler”
nor an “industrial furnace”.that:
Uses controlled flame combustion and neither:
Meets the criteria for classification as
a
boiler.
sludae dryer or carbon regeneration
unit, nor
Is
listed
as
an
industrial
furnace;
or
Meets
the
definition
of
infrared
incinerator
or
plasma
arc
incinerator.
128—528
59
“Incompatible waste” means a hazardous waste which is
suitable for:
Placement in
a particular device or facility
because it may cause corrosion or decay of
containment
materials
(e.g.,
container
inner
liners or tank walls); or
Commingling
with
another
waste
or
material
under
uncontrolled conditions because the commingling
might produce heat or pressure, ‘fire or explosion,
violent reaction, toxic dusts, mists,
fumes or
gases or flammable fumes or gases.
(See 35 111.
Ada. Code 725~.AppendixE for
examples.)
“Industrial
furnace”
means
any
of
the
following
enclosed devices that are’integral components of
manufacturing
processes
and
that
use
controlled
flame
devicesthermal
treatment
to
accomplish
recovery
of
materials
or
energy:
Cement
kilns
Lime
kilns
Aggregate
kilns
Phosphate
kilns
Coke
ovens
Blast
furnaces
Smelting, melting and refining furnaces
(including
pyrometallurgical devices such as cupolas,
reverberator furnaces, sintering machines,
roasters and foundry furnaces)
Titanium dioxide chloride process oxidation
reactors
Methane reforming furnaces
Pulping liquor recovery furnaces
Combustion devices used in the recovery of sulfur
values from spent sulfuric acid
H~1ogenacid furnaces (HAFs)
for the production of
128—529
60
acid from halo~enatedhazardous waste generated by
chemical production facilities where the furnace
is
located
on
the
site
of
a
chemical
production
facility, the acid product has a halogen acid
content of at least 3.
the acid product is used
in a manufacturina process and, except for
hazardous waste burned as fuel, hazardous waste
fed to the furnace has a minimum halogen content
of 20.
as generated.
Any other such device as the Agency determines to
be
an
“Industrial
Furnace”
on
the
basis
of
one
or
more of the following factors:
The design and use of the device primarily to
accomplish recovery of material products;
The use of the device to burn or reduce raw
materials to make a material product;
The use of the device to burn or reduce
secondary materials as effective substitutes
for raw materials,
in processes using raw
materials as principal feedstocks;
The
use
of
the
device
to
burn
or
reduce
secondary materials as ingredi.ents in an
industrial process to make a material
product;
The use of the device in common industrial
practice to produce a material product; and
Other relevant factors.
“Individual generation site” means the contiguous site
at or on which one or more hazardous wastes are
generated.
An individual generation site, such as a
large manufacturing plant, may have one or more sources
of hazardous waste but is considered a single or
individual generation site if the site or property is
contiguous.
“Infrared incinerator” means any enclosed device which
uses electric powered resistance heaters as a source of
radiant heat and which is not listed as an industrial
furnace.
“Inground tank” means a device meeting the definition
of “tank” whereby a portion of the tank wall is
situated to any degree within the ground, thereby
preventing visual inspection of that external surface
128—530
61
area of the tank that is in the ground.
“In
operation”
refers
to
a
facility
which
is
treating,
storing
or
disposing
of
hazardous
waste.
“Injection
well”
means
a
well
into
which
fluids
are
being injected.
(See also “underground injection”.)
“Inner
liner”
means
a
continuous
layer
of
material
placed inside a
tank
or container which protects the
construction
materials
of
the
tank
or
container
from
the
contained
waste
or
reagents
used
to
treat
the
waste.
“Installation
inspector”
means
a
person
who,
by
reason
of
knQwledge
of
the
physical
sciences
and
the
principles
of
engineering,
acquired
by
a
professional
education
and
related
practical
experience,
is
qualified
to
supervise
the
installation
of
tank
systems.
“International
shipment”
means
the
transportation
of
hazardous
waste
into
or
out
of
the
jurisdiction
of
the
United
States.
“Land
treatment
facility”
means
a
facility
or
part
of
a
facility
at
which
hazardous
waste
is
applied
onto
or
incorporated into the soil surface; such facilities are
disposal
facilities
if
the
waste
will
remain
after
closure.
“Landfill”
means
a
disposal
facility
or
part
of
a
facility
where
hazardous
waste
is
placed
in
or
on
land
and
which
is
not
a
pile,
a
land
treatment
facility,
a
surface
impoundment,
an
underground
injection
well,
a
salt dome formation, an underground mine or a cave.
“Landfill cell” means a discrete volume of a hazardous
waste
landfill
which
uses
a
liner
to
provide
isolation
of wastes from adjacent cells or wastes.
Examples of
landfill cells .are trenches and pits.
“Leachate” means any liquid,
including any suspended
components in the liquid, that has percolated through
or drained from hazardous waste.
“Liner” means a continuous layer of natural or manmade
materials
beneath
or
on
the
sides
of
a
surface
impoundment,
landfill
or
landfill
cell,
which
restricts
the downward or lateral escape of hazardous waste,
hazardous waste constituents or leachate.
128—53 1
62
“Leak—detection system” means a system capable of
detecting the failure of either the primary or
secondary
containment
structure
or
the
presence
of
a
release
of
hazardous
waste
or
accumulated
liquid
in
the
secondary containment structure.
Such
a system must
employ operational controls (e.g.,
daily visual
inspections for releases into the secondary containment
system of aboveground tanks)
or consist of an
interstitial monitoring device designed to detect
continuously and automatically the failure of the
primary or secondary containment structure or the
presence of a release
of’ hazardous waste into the
secondary containment structure.
“Management” or “hazardous waste management” means the
systematic control of the collection,
source
separation,
storage, transportation, processing,
treatment,
recovery
and
disposal
of
hazardous
waste.
“Manifest” means the shipping document originated and
signed by the generator which contains the information
required
by
35
Ill.
Ada.
Code
722.Subpart
B.
“Manifest document number” means the USEPA twelve digit
identification’
number
assigned
to
the
generator
plus
a
unique five digit document number assigned to the
manifest
by
the
generator
for
recording
and
reporting
purposes.
“Mining overburden returned to the mine site” means any
material overlying an economic mineral deposit which is
removed to gain access to that deposit and is then used
for
reclamation
of
a
surface
mine.
“Miscellaneous unit” means a hazardous waste management
unit where hazardous waste is treated,
stored or
disp6sed of and which is not a container,
tank, tank
system, surface impoundment, pile,
land treatment unit,
landfill, incinerator, boiler, industrial furnace,
underground injection well with appropriate technical
standards under 35 Ill. Ads. Code 730, or a unit
eligible for a research, development and demonstration
permit under 35 Ill.
Ada.
Code 703.231.
“Movement” means that hazardous waste transported to a
facility in an individual vehicle.
“New hazardous waste management facility” or “new
facility” means a facility which began operation,
or
for which construction commenced, after November 19,
1980.
(See also “Existing hazardous waste management
facility”.)
128—5 32
63
“New tank system” or “new tank component” means
a tank
system or component that will be used for the storage
or treatment of hazardous waste and for which
installation commenced after July 14,
1986; except,
however,
for purposes of 35 Ill.
Ada.
Code
724.293(g) (2) and 725.293(g) (2),
a new tank system is
one for which construction commences after July 14,
1986.
(See also “existing tank system.”)
“Onground tank” means a device meeting the definition
of
“tank”
that
is
situated
in
such
a
way
that
the
bottom
of
the
tank
is
on
the
same
level
as
the
adjacent
surrounding surfaces so that the external tank bottom
cannot
be
visually
inspected.
“On—site”
means
the
same
or
geographically
contiguous
property
which
may
be
divided
by public or private
right—of—way,
provided
the
entrance
and
exit
between
the
properties
is
at
a
crossroads
intersection
and
access
is by crossing as opposed to going ‘along the
right-of—way.
Noncontiguous
properties
owned
by
the
same
person
but
connected
by
a
right—of—way
which
he
controls
and
to
which
the
public
does
not
have
access
is
also
considered
on-site
property.
“Open
burning”
means
the
combustion
of
any
material
without
the
following
characteristics:
Control
of
combustion
air
to
maintain
adequate
temperature
for
efficient
combustion;
Containment
of
the
combustion
reaction
in
an
enclosed device to provide sufficient residence
time
and
mixing
for
complete
combustion;
and
Control
of
emission
of
the
gaseous
combustion
products.
(See
also
“incineration”
and
“thermal
treatment”.)
“Operator” means the person responsible for the overall
operation of a facility.
“Owner”
means the person who owns a facility or part of
a
facility.
“Partial closure” means the closure of a hazardous
waste management unit in accordance with the applicable
closure
requirements
of
35
Ill.
Ada.
Code
724
or
725
at
a
facility
which
contains
other
active
hazardous
waste
management units.
For example, partial closure may
128—533
64
include
the
closure
of
a
tank
(including
its
associated
piping
and underlyi’ng containment systems), landfill
cell, surface impoundment, waste pile or other
hazardous waste management unit,
while other units of
the same facility continue to operate.
“Person” means an individual,
trust,
firm,
joint stock
company, federal agency,’ corporation (including a
government
corporation),
partnership,
association,
state, municipality, commission, political subdivision
of a state or any interstate body.
“Personnel” or “facility personnel” means all persons
who work at or oversee the operations of a hazardous
waste
facility
and
whose
actions
or
failure
to
act
may
result
in
noncompliance
with
the
requirements
of,
35
Ill.
Adm.
Code
724
or
725.
“Pile” means any noncontainerized accumulation of
solid,
non-flowing hazardous waste that is ‘used for
treatment
or
storage.
“Plasma
arc
incinerator”
means
any enclosed device
which
uses
a
high
intensity
electrical
discharge
or
arc
as
a
source
of
heat
and
which
is
not
listed
as
an
industrial furnace.
“Point source” means any discernible, confined and
discrete
conveyance
including,
but
not
limited
to,
any
pipe,
ditch, channel,
tunnel, conduit, well, discrete
fissure, container, rolling stock, concentrated animal
feeding operation or vessel or other floating craft
from which pollutants are or may be discharged.
This
term
does
not include return flows from irrigated
agriculture.
“Publicly
owned
treatment
works”
or
“POTW”
is
as
defined in 35 Ill. Ada.
Code 310.110.
“Regional Administrator” means the Regional
Administrator for the EPA Region in which the facility
is located or the Regional Administrator’s designee.
“Representative sample” means a sample of a universe or
whole
(e.g., waste pile,
lagoon,
groundwater) which can
be expected to exhibit the average properties of the
universe or whole.
“Runoff” means any rainwater,
leachate or other liquid
that
drains
over
land
from
any
part
of
a
facility.
“Runon” means any rainwater,
leachate or other liquid
128—534
65
that
drains
over
land
onto
any
part
of
a
facility.
“Saturated zone” or “zone of saturation” means that
part of the earth’s crust in which all voids are filled
with
water.
“SIC Code” means Standard Industrial Code as defined in
Standard Industrial Classification Manual, ‘incorporated
by reference in Section 720.111.
“Sludge” means any solid, semi—solid or liquid waste
generated from a municipal,
commercial or industrial
wastewater treatment plant, water supply treatment
plant or air pollution control facility exclusive of
the treated effluent from a wastewater treatment plant.
“Sludge dryer” means any enclosed thermal treatment
device which is used to dehydrate sludge and which has
a total thermal input, excluding the heating value’ of
the sludge itself, of 2500 Btu/lb or less of sludge
treated
on
a
wet
weight
basis.
“Small
Quantity
Generator”
means
a
generator
which
generates less than 1000 kg of hazardous waste in a
calendar
month.
“Solid waste” means a solid waste as defined in 35 Ill.
Ada.
Code
721.102.
“Sump” means any pit or reservoir that meets the
definition
of
tank
and
those
troughs
or
trenches
connected
to
it
that
serve
to
collect
hazardous
waste
for transport to hazardous waste storage, treatment or
disposal facilities.
“State”
means
any
of
the
several
states,
the
District
of Columbia, the Commonwealth of Puerto Rico, the
Virgin Islands,
Guam, American Samoa and the
Commonwealth
of
the
Northern
Mariana
Islands.
“Storage” means the holding of hazardous waste for a
temporary period, at the end of which the hazardous
waste is treated, disposed of or stored elsewhere.
“Surface impoundment” or “impoundment” means a facility
or
part
of
a
facility
which
is.
a
natural
topographic
depression, manmade excavation or diked area formed
primarily of earthen materials (although it may be
lined
with
manmade
materials)
which
is
designed
to
hold
an accumulation of liquid wastes or wastes containing
free
liquids
and
which
is
not
an
injection
well.
Examples
of
surface
impoundments
are
holding,
storage,
128—535
66
settling and aeration pits,
ponds and lagoons.
“Tank”
means
a
stationary
device,
designed
to
contain
an accumulation of hazardous waste which is constructed
primarily
of
nonearthen
materials
(e.g.,
wood,
concrete,
steel,
plastic) which provide structural
support.
“Tank system” means a hazardous waste storage or
tre&tment tank and its associated ancillary equipment
and containment system.
“Thermal treatment” means the treatment of hazardous
waste in a device which uses elevated temperatures as
the primary means to change the chemical, physical or
biological character or composition of the hazardous
waste.
Examples
of
thermal
treatment
processes
are
incineration, molten salt, pyrolysis,
calcination, wet
air oxidation and microwave discharge.
(See also
“incinerator”
and
“open
burning”.)
“Totally
enclosed
treatment
facility”
means
a
facility
for the treatment of hazardous waste which is directly
connected
to
an
industrial
production
process
and
which
is
constructed
and
operated
in
a
manner
which
prevents
the
release
of
any
hazardous
waste
or
any
constituent
thereof into the environment during treatment.
An
example is a pipe in which waste acid is neutralized.
“Transfer
facility”
means
any
transportation
related
facility including loading docks, parking areas,
storage areas and other similar areas where shipments
of hazardous waste are held during the normal course of
transportation.
“Transport vehicle” means a motor vehicle or rail car
used
for
the
transportation
of
cargo
by
any
mode.
Each
cargo—carrying
body
(trailer,
railroad
freight
car,
etc.)
is a separate transport vehicle.
“Transportation” means the movement of hazardous waste
by air, rail,
highway or water.
“Transporter” means a person engaged in the off—site
transportation of hazardous waste by
air,.., rail, highway
or
water.
“Treatability study” means:
A study in which a hazardous waste is subjected to
a treatment process to determine:
128—536
67
Whether
the waste is amenable to the
treatment process.
What
pretreatment (if any)
is required.
The
optimal
process conditions needed to
achieve the desired treatment.
The efficiency of a treatment process for a
specific waste or wastes.
Or,
The characteristics and volumes of residuals
from a particular treatment process.
Also included in this definition for the purpose
of 35
Ill. Adm. Code 721.104(e)
and
(f) exemptions
are liner compatibility, corrosion and other
material
compatibility
studies
and
toxicological
and health effects studies.
A “treatability
study” is not a means to commercially treat or
dispose
of
hazardous
waste.
“Treatment” means any method, technique or process,
including neutralization,
designed to change the
physical, chemical or biological character or
composition
of
any
hazardous
waste
so
as
to
neutralize
such waste, or so as to recover energy or material
resources from the waste or so as to render such waste
non—hazardous or less hazardous; safer to transport,
store or dispose of; or amenable for recovery, amenable
for storage or reduced in volume.
“Treatment zone” means a soil area of the unsaturated
zone
of
a
land
treatment
unit
within
which
hazardous
constituents are degraded, transformed or immobilized.
“Underground injection” means the subsurface
emplacement of fluids through a bored,
drilled or
driven well; or through
a dug well,
where the depth of
the dug well is greater than the largest surface
dimension.
(See also “injection well”.)
“Underground tank” means a device meeting the
definition of “tank” whose
entir.e surface area is
totally
below
the
surface
of
and
covered
by
the
ground.
“Unfit-for—use tank system” means a tank system that
has been determined through an integrity assessment or
other
inspection
to
be
no
longer
capable
of
storing
or
treating hazardous waste without posing
a threat of
release of hazardous waste to the environment.
128—53 7
68
“Uppermost aquifer” means the geologic formation
nearest
the
natural
ground
surface
that
is
an
aquifer,
as well as lower aquifers that are hydraulically
interconnected with this aquifer within the facility’s
property boundary.
“United
States”
means
the
50
States,
the
District
of
Columbia, the Commonwealth of Puerto Rico,
the U.S.
Virgin Islands, Guam, American Samoa and the
Commonwealth of the Northern Mariana Islands.
“Unsaturated zone” or “zone of aeration” means the zone
between the land surface and the water table.
“USEPA” means United States Environmental Protection
Agency.
“Vessel” includes every description of watercraft,
used
or capable of being used as a means of transportation
on the water.
“Wastewater
treatment
unit”
means
a
device
which:
Is
part
of
a
wastewater
treatment
facility
which
has an NPDES permit pursuant to 35 Ill. Adm. Code
309 or a pretreatment permit or authorization to
discharge pursuant to 35 Ill.
Ada. Code 310; and
Receives and treats or stores an influent
wastewater
which
is
a
hazardous
waste
as
defined
in
35
Ill.
Adm.
Code
721.103,
or
generates
and
accumulates a wastewater treatment sludge which is
a hazardous waste as defined in 35 Ill.
Ada.
Code
721.103, or treats or stores a wastewater
treatment sludge which is a hazardous waste as
defined
in
35
Ill.
Ada.
Code
721.103;
and
Meets the definition of tank or tank system in
this Section.
“Water
(bulk shipment)” means the bulk transportation
of hazardous waste which is loaded or carried on board
a vessel without containers or labels.
“Well” means any shaft or pit dug or bored into the
earth, generally of a cylindrical form,
and often
walled with bricks or tubing to prevent the earth from
caving in.
“Well
injection”
(See
“underground
injection”).
“Zone of engineering control” means an area under the
1
28—5~3d
69
control
of
the
owner
or
operator
that,
upon
detection
of
a
hazardous
waste
release,
can
be
readily
cleaned
up
prior to the release of hazardous waste or hazardous
constituents to groundwater or surface .water.
(Source:
Amended at
Ill.
Reg.
,
effective
)
Section
720.111
References
a)
The
following
publications
are
incorporated
by
reference:
ANSI.
Available from the American National
Standards Institute, 1430 Broadway, New York, New
York
10018,
(212)
354—3300:
ANSI
B31.3
and
B31.4.
See
ASME/ANSI
B31.3
and B31.4
ACI.
Available
from
the
American
Concrete
Institute,
Box
19150,
Redford
Station,
Detroit,
Michigan
48219:
ACI 318—83:
“Building Code Requirements for
Reinforced Concrete”,
adopted
September,
1983.
API.
Available
from
the
American
Petroleum
Institute,
1220
L
Street,
N.W.,
Washington,
D.C.
20005,
(202)
682—8000:
“Guide for Inspection of Refinery Equipment,
Chapter XIII, Atmospheric and Low Pressure
Storage Tanks,”
4th
Edition,
1981,
reaffirmed
December,
1987.
“Cathodic Protection of Underground Petroleum
Storage Tanks and Piping Systems,” API
Recommended Practice 1632, Second Edition,
December,
1987.
“Installation of Underground Petroleum
Storage Systems,”
API
Recommended Practice
1615,
Fourth
Edition,
November,
1987.
APTI.
Available from the Air and Waste Management
Association, Box 2861, Pittsburgh,
PA
15230,
(412)
232—3444:
APTI Course 415:
Control of Gaseous
Emissions,
EPA
Publication
EPA—450/2—81-005,
128—539
70
December,
1981.
ASME.
Available from the American Society of
Mechanical Engineers,
345 East 47th Street, New
York,’ NY
10017,
(212)
705—7722:
“Chemical Plant and Petroleum Refinery
Piping”, ASMEIANSI 331.3—1987,
as
supplemented by B31.3a—1988 and B31.3b—1988.
Also available from ANSI.
“Liquid
Transportation Systems for
Hydrocarbons, Liquid Petroleum Gas, Anhydrous
Ammonia,
and Alcohols”, ASME/ANSI B3l.4-1986,
as supplemented by B31.4a—1987.
Also
available from ANSI.
ASTM.
Available from American Society for Testing
and Materials,
1916 Race Street, Philadelphia, PA
19103,
(215)
299—5400:
ASTM C94-90, Standard Specification for
Ready-Mixed Concrete, approved March 30,
1990.
ASTN
D93-85, Standard Test Methods for Flash
Point by Pensky-Martens Closed Testerapproved
October 25,
1985.
ASTM
D1946—90,
Standard
Practice
for
Analysis
of
Reformed
Gas
by
Gas
Chromatography,
Approved March 30,
1990.
ASTM
D2267-88, Standard Test Method for
Aromatics
in
Light
Naphthas
and
Aviation
Gasolines by Gas Chromatography, approved
November 17,
1988.
ASTM
D2382-88, Standard Test Method for Heat
of Combustion of Hydrocarbon Fuels by Bomb
Calorimeter (High Precision Method), approved
October 31,
1988.
ASTM
D2879-86, Standard Test Method for Vapor
Pressure—Temperature Relationship and Initial
Decomposition Temperature of Liquids by
Isoteniscope, approved October
31,
1986.
ASTM D3828-87, Standard Test Methods for
Flash Point of Liquids by Setaflash Closed
Tester, approved December 14,
1988.
128—540
71
ASTM
E168-88,
Standard
Practices
for
General
Techniques
of
Infrared
Quantitative
Analysis,
approved May 27, 1988.
ASTM
El69—87, Standard Practices for General
Techniques of Ultraviolet-Visible
Quantitative Analysis, approved February 1,
1987.
ASTM
E260-85, Standard Practice for Packed
Column
Gas
Chromatography,
approved
June
28,
1985.
GPO.
Available from the Superintendent of
Documents, U.S. Government Printing Office,
Washington,
D.C.
20401,
(.202)
783—3238:
Standard
Industrial
Classification
Manual
(1972),
and
1977
Supplement,
republished’
in
1983
NACE.
Available
from
the
National
Association
of
Corrosion
Engineers,
1400
South
Creek
Dr.,
Houston,
TX
77084,
(713)
492—0535:
“Control
of
External
Corrosion
on
Metallic
Buried,
Partially
Buried,
or
Submerged
Liquid
Storage
Systems”,
NACE
Recommended
Practice
RP0285—85,
approved March,
1985.
NFPA.
Available
from
the
National
Fire
Protection
Association,
Batterymarch
Park,
Boston,
MA
02269,
(617)
770—3000
or
(800)
344—3555:
“Flammable
and
Combustible
Liquids
Code”
NFPA
30,
issued
July
17,
1987.
Also
available
from
ANSI.
NTIS.
Available
from
the
National
Technical
Information Service,
5285 Port Royal Road,
Springfield, VA
22161,
(703) 487—4600:
“Generic
Quality
Assurance
Project
Plan
for
Land
Disposal
Restrictions
Program”,
EPA/530-
SW-87-011, March 15,
1987.
(Document number
PB 88—170766.)
“Guidance on Air Quality Models”, Revised
1986.
(Document number PB86—245—248
(Guideline)
and
PB88-150—958
(Supplement)).
“Methods
for
Chemical
Analysis
of
Water
and
128—541
72
Wastes”,
Third
Edition,
March,
1983.
(Document
number
PB
84—128677)
“Methods Manual for Compliance with BIF
Regulations”. December. 1990.
(Document
number
PB91—120—006)
“Petitions to Delist Hazardous Wastes
--
A
Guidance Manual”,
EPA/530—SW—85—003, April,
1985.
(Document Number PB 85—194488
“Procedures Manual for Ground Water
Monitoring at Solid Waste Disposal
Facilities”, EPA—530/SW—611,
1977.
(Document
number
PB 84-174820)
“Screening Procedures for Estimating the Air
Quality Impact of Stationary Sources”.
August.
1988 (Document number PB89-159396).
“Test Methods for Evaluating Solid Waste,
Physical/Chemical Methods,” EPA Publication
number SW-846
(Second Edition,
1982 as
amended
by
Update
I
(April,
1984)
and
Update
II’ (April,
1985))
(Document number PB 87-
120291)
STI.
Available from the Steel Tank Institute,
728
Anthony Trail,
Northbrook,
IL
60062,
(312)
498-
1980:
“Standard for Dual Wall Underground Steel
Storage Tanks”
(1986).
USEPA.
Available
from
United
States
Environmental
Protection Agency, Office of Drinking Water,
State
Programs Division, WH 550 E, Washington,
D.C.
20460:
“Technical Assistance Document:
Corrosion,
Its Detection and Control in Injection
Wells”, EPA 570/9—87—002, August,
1987.
USEPA.
Available
from
USEPA,
Number
F-90-WPWF-
FFFFF, Room M2427,
401 M Street SW, Washington,
D.C.
20460,
(202)
475—9327:
“Test
Method
8290:
Procedures
for
the
Detection and Measurement of PCDD5 and
PCDF5”, EPA/530—SW—91—019
(January,
1991)
b)
Code of Federal Regulations.
Available from the
128—542
73
Superintendent
of
Documents,
U.S.
Government
Printing
Office,
Washington,
D.C.
20401,
(202)
783—3238:
10
CFR
20,
Appendix
B
(19901991)
40 CFR 51.100(u)
(1991)
40 CFR 60
(19901991)
40
CFR
61,
Subpart
V
(19901991)
40
CFR
136
(19901991)
40 CFR 142
(19901991)
40
CFR
220
(19901991)
40
CFR
260.20
(19901991)
40
CFR
264
(19901991)
40
CFR
302.4,
302.5
and
302.6
(19901991)
40
CFR
761
(19901991)
c)
Federal
Statutes
Section 3004 of the Resource Conservation and Recovery
Act
(42
U.S.C.
6901
et
seq.),
as
amended
through
December
31,
1987.
d)
This Section incorporates no later editions or
amendments.
(Source:
Amended
at
Ill.
Reg.
,
effective
)
128—543
74
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION
CONTROL
BOARD
SUBCHAPTER
c:
HAZARDOUS
WASTE OPERATING REQUIREMENTS
PART
721
IDENTIFICATION
AND
LISTING OF HAZARDOUS WASTE
SUBPART
A:
GENERAL
PROVISIONS
Section
721.
101
721.
102
721.
103
721.
104
721.105
721. 106
721.107
721.108
Purpose and Scope
Definition of Solid Waste
Definition of Hazardous Waste
Exclusions
Special Requirements for Hazardous Waste Generated by
Small
Quantity
Generators
Requirements
for
Recyclable
Materials
Residues of Hazardous Waste in Empty Containers
PCB Wastes Regulated underTSCA
SUBPART B:
CRITERIA FOR IDENTIFYING THE CHARACTERISTICS
OF
HAZARDOUS
WASTE
AND
FOR
LISTING
HAZARDOUS
WASTES
Criteria for Identifying the Characteristics of
Hazardous Waste
721.111
Criteria
for
Listing
Hazardous
Waste
SUBPART
C:
CHARACTERISTICS
OF
HAZARDOUS
WASTE
Section
721.
120
721.121
721.
122
721.123
721.
124
General
Characteristic of Ignitability
Characteristic of Corrosivity
Characteristic of Reactivity
Toxicity Characteristic
SUBPART D:
LISTS OF HAZARDOUS WASTE
Section
721.130
General
721.131
Hazardous Wastes From Nonspecific Sources
721.132
Hazardous Waste from Specific Sources
721.133
Discarded Commercial Chemical Products, Off—
Specification Species, Container Residues and Spill
Residues Thereof
721.135
Wood
Preserving
Wastes
Representative Sampling Methbds
Method 1311 Toxicity Characteristic Leaching
Procedure (TCLP)
Chemical Analysis Test Methods
Analytical Characteristics of Organic Chemicals
(Repealed)
Analytical
Characteristics
of
Inorganic
Species
Section
721. 110
Appendix A
Appendix B
Appendix
C
Table
A
Table
B
128—544
75
(Repealed)
Table C
Sample Preparation/Sample Introduction Techniques
(Repealed)
Appendix G
Basis for Listing Hazardous Wastes
Appendix H
Hazardous Constituents
Appendix
I
Wastes
Excluded
under
Section
720.120
and
720.122
Table A
Wastes Excluded from Non-Specific Sources
Table
B
Wastes
Excluded
from
Specific
Sources
Table
C
Wastes
Excluded
From
Commercial
Chemical
Products,
Off-Specification Species, Container Residues, and
Soil Residues Thereof
Appendix 3
Method of Analysis for Chlorinated Dibenzo-p-
Dioxins and Dibenzofurans
Appendix
Z
Table to Section 721.102
AUTHORITY:
Implementing
Section
22.4
and
authorized
by
Section
27
of
the
Environmental
Protection
Act
(Ill.
Rev.
Stat.
1989,
ch.
111½,pars.
1022.4
and
1027).
SOURCE:
Adopted
in
R81-22,
43
PCB
427,
at
5
Ill.
Reg.
9781,
effective
as
noted
in
35
Ill.
Ada.
Code
700.106;
amended
and
codified in R81—22,
45 PCB 317, at 6 Ill.
Reg. 4828,
effective as
noted in 35 Ill. Adm. Code 700.106; amended in R82—18,
51 PCB 31,
at
7
Ill.
Reg.
2518,
effective
February
22,
1983;
amended
in
R82-
19,
53
PCB
131,
at
7
Ill.
Reg.
13999,
effective
October
12,
1983;
amended
in
R84—34,
61
PCB
247,
at
8
Ill
Reg.
24562,
effective
December
11,
1984;
amended
in
R84-9,
at
9
Ill.
Reg.
11834,
effective
July
24,
1985;
amended
in
R85—22
at
10
Ill.
Reg.
998,
effective
January
2,
1986;
amended
in
R85—2
at
10
Ill.
Reg.
8112,
effective
May
2,
1986;
amended
in
R86—1
at
10
Ill.
Reg.
14002,
effective
August
12,
1986;
amended
in
R86—19
at
10
Ill.
Reg.
20647,
effective
December
2,
1986;
amended
in
R86—28
at
11
Ill.
Reg.
6035,
effective
March
24,
1987;
amended
in
R86—46
at
11
Ill.
Reg.
13466,
effective
August
4,
1987; amended in R87—32 at 11
Ill.
Reg.
16698,
effective
September
30,
1987;
amended
in
R87—5
at
11
Iii.
Reg.
19303,
effective
November
12,
1987;
amended
in
R87—26
at
12
Ill.
Reg.
2456,
effective
January
15,
1988;
amended
in
R87—30
at
12
Ill.
Reg.
12070,
effective
July
12,
1988;
amended
in
R87—39
at
12
Ill.
Reg.
13006,
effective
July
29,
1988;
amended
in
R88-16
at
13
Ill.
Reg.
382,
effective
December
27,
1988;
amended
in
R89—1
at
13
Ill.
Reg.
18300,
effective
November
13,
1989;
amended
in
R90—2
at
14
Ill.
Reg.
14401,
effective
August
22,
1990; amended in R90—10 at 14 Ill. Reg.
16472, effective
September 25,
1990;
amended in R90-17 at 15 Ill. Reg.
7950.,
effective May 9,
1991; amended in R90—ll at 15 Ill. Reg.
9332,
effective
June
17,
1991;
amended
in
R91-’l at 15 Ill. Reg.
14473,
effective
October
1,
1991;
amended
in
R91—13
at
16
Ill.
Reg.
,
effective
SUBPART A:
GENERAL
PROVISIONS
Section
721.102
Definition
of
Solid
Waste
128—545
76
a)
Solid waste.
1)
A
solid
waste
is
any
discarded
material
that
is
not
excluded
by
Section
721.104(a)
or
that
is
not
excluded
pursuant
to
35
Ill.
Ada.
Code
720.130
and
720.131.
2)
A discarded material is any material which is:
A)
Abandoned, as explained in subsection
(b); or
B)
Recycled,
as
explained
in
subsection
(c);
or
C)
Considered
inherently
waste-like,
as
explained
in
subsection
(d).
b)
Materials
are solid waste if they are abandoned by
being:
1)
Disposed
of;
or
2)
Burned or incinerated; or
3)
Accumulated, stored or treated
(but not recycled)
before
or
in
lieu
of
being
abandoned
by
being
disposed
of,
burned
or
incinerated.
c)
Materials
are solid wastes if they are recycled
——
or
accumulated,
stored
or
treated
before
recycling
——
as
specified
in
subsections
(c)
(1)
through
(c)
(4)
if
they
are:
1)
Used in a manner constituting disposal.
A)
Materials noted with a “yes” in column
1
of
table in Appendix
Z are solid wastes when
they are:
i)
Applied
to
or
placed
on
the
land
in
a
manner that constitutes disposal; or
ii)
Used
to
produce
products
that
are
applied
to
or
placed on the land orare
otherwise
contained
in
products
that
are
applied to or placed on the land (in
which cases the product
itself
remains
a
solid waste).
B)
However, commercial chemical products listed
in
Section
721.133
are not solid wastes if
they
are
applied
to
the
‘land
and
that
is
128—546
77
their ordinary manner of use.
2)
Burned for energy recovery.
B)
Materials noted with a “yes”
in column
2 of
table in Appendix Z are solid wastes when
they are:
i)
burned to recover energy;
ii)
Used to produce a fuel or are otherwise
contained in fuels
(in which case the
fuel itself remains a solid waste);
iii) Contained in fuels
(in which case the
fuel
itself
remains
a
solid
waste).
B)
However,
commercial
chemical
products
listed
in
Section
721.133
are
not
solid
wastes
if
they are themselves fuels.
3)
Reclaimed.
Materials
noted
with
a
“yes”
in
column
3 of table
in Appendix Z are solid wastes when
reclaimed.
4)
Accumulated
speculatively.
Materials
noted
with
“yes”
in column
4 of table in Appendix
Z are solid
wastes
when
accumulated
speculatively.
d)
Inherently
waste-like
materials.
The
following
materials are solid wastes when they are recycled in
any manner:
1)
Hazardous waste numbers F020,
F021 (unless used as
an
ingredient
to
make
a
product
at
the
site
of
generation),
F022, F023,
F026 and F028.
21
Secondary materials fed to a halogen acid furnace
that exhibit a characteristic of a hazardous waste
or are listed as a hazardous waste as defined in
Subparts C~or
D. except for brpminated material
which meets the following criteria:
~j.
The material must contain a bromine
concentration of at least 45;
and
~j
The material must contain less than a total
of
1
of toxic organic compounds listed in
Appendix H;
and
~j
The material is processed continually on—site
in the halogen acid furnace via direct
128—547
78
con’~.’eyance (hard
piping).
~)
The
following
criteria
are
used
to
add
wastes
to
the list:
a)
Disposal method or toxicity.
i)
The materials are ordinarily disposed
of, burned or incinerated; or
ii)
The materials contain toxic constituents
listed in Appendix H and these
constituents are not ordinarily found in
raw materials or products for which the
materials substitute
(or are found in
raw materials or products in smaller
concentrations)
and are not used or
reused during the recycling process; and
B)
The material may pose a substantial hazard to
human
health
and
the
environment
when
recycled.
e)
Materials
that
are
not
solid
waste
when
recycled.
1)
Materials are not solid wastes when they can be
shown to be recycled by being:
A)
Used or reused as ingredients in an
industrial
process
to
make
a
product,
provided
the
materials
are
not
being
reclaimed;
or
B)
Used or reused as effective substitutes for
commercial products; or
C)
Returned to the original process from which
they are generated, without first being
reclaimed.
The materials must be returned as
a substitute for raw materials feedstock,
and
the process must use raw materials as
principal feedstocks.
2)
The following materials are solid wastes, even if
the recycling involves use, reuse or return to the
original process (described in subsections
(e) (1) (A)—(C):
A)
Materials used in a manner constituting
disposal, or used to produce products that
are applied to the land;
or
128—548
79
B)
Materials burned for energy recovery, used to
produce
a
fuel
or
contained
in
fuels;
or
C)
Materials accumulated speculatively;
or
D)
Materials listed in subsection
(d) (1).
f)
Documentation of claims that materials are not solid
wastes
or
are
conditionally
exempt
from
regulation.
Respondents in actions to enforce regulations
implementing Subtitle C of the Resource Conservation
Recovery Act or Section 21 of the Environmental
Protection Act who raise a claim that a certain
material is not a solid waste,
or is conditionally
exempt from regulation must demonstrate that there
is a
known
market or disposition for the material, and that
they meet the terms of the exclusion or exemption.
In
doing
so,
they
must
provide
appropriate
documentation
(such
as
contracts
showing
that
a
second
person
uses
the
material
as
an
ingredient
in
a
production
process)
to
demonstrate
that
the
material
is
not
a
waste,
or
is
exempt from regulation.
In addition, owners or
operators
of
facilities
claiming that they actually are
recycling materials must show that they have the
necessary equipment to do so.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section
721.103
Definition
of
Hazardous
Waste
a)
A solid waste, as defined in Section 721.102,
is a
hazardous
waste
if:
1)
It
is
not
excluded
from
regulation
as
a
hazardous
waste under Section 721.104(b); and
2)
It meets any of the following criteria;
A)
It exhibits any of the characteristics of
hazardous waste identified in Subpart
C.
Except that any mixture of a waste from
the
extraction, beneficiation or processing of
ores or minerals excluded under Section
721.104(b) (7)
and any other solid waste
exhibiting a characteristic ‘of hazardous
waste under Subpart C is a hazardous waste
only:
if it exhibits a characteristic that
would not have been exhibited by the excluded
waste alone if such mixture had not occurred;
or,
if it continues to exhibit any of the
characteristics
exhibited
by
the
non-excluded
128—549
80
wastes prior to mixture.
Further,
for the
purposes of applying the EP toxicity
(extraction procedure toxicity),
characteristic to such mixtures, the mixture
is
also
a’ hazardous waste:
if it exceeds the
maximum concentration for any contaminant
listed in Section 721.124 that would not have
been exceeded ~bythe excluded waste alone if
the mixture had not occurred; or,
if it
continues to exceed the maximum concentration
for any contaminant exceeded by the nonexempt
waste prior to mixture.
B)
It is listed in Subpart D and has not been
excluded from the lists in Subpart D under 35
Ill. Ada. Code 720.120 and 720.122.
C)
It is a mixture of a solid waste and a
hazardous waste that is listed in Subpart D
solely because it exhibits one or more of the
characteristics of hazardous waste identified
in Subpart C,
unless the resultant mixture no
longer exhibits any characteristic of
hazardous waste identified in Subpart C, or
unless the solid waste:
is excluded from
regulation under Section 721.104(b) (7); and,
the resultant mixture no longer exhibits any
characteristic of hazardous waste identified
in Subpart C for which the hazardous waste
listed
in
Subpart
D
was
listed.
D)
It is a mixture of solid waste and one or
more hazardous wastes listed in Subpart D and
has not been excluded from this paragraph
under 35 Ill. Ada. Code 720.120 and 720.122;
however, the following mixtures of solid
wastes and hazardous wastes listed in Subpart
D are not hazardous wastes
(except by
application of subsection (a)(2)(A) or (B))
if the generator can demonstrate that the
mixture consists of wastewater the discharge
of which is subject to regulation under
either 35 Ill.
Ada.
Code 309 or 310
(including wastewater at facilities which
have eliminated the discharge of wastewater)
and;
i)
One or more of the following spent
solvents listed in Section 721.131
—
carbon tetrachloride, tetrachioro
ethylene, trichloroethylene
-
provided
that the maximum total weekly usage of
128—550
81
these solvents (other than the amounts
that can be demonstrated not to be
discharged to wastewater)
divided by the
average weekly flow of wastewater into
the headworks of the facility’s
wastewater treatment or pre—treatment
system
does
not
‘exceed
1
part
per
million;
or
ii)
One or more of the following spent
solvents listed in Section 721.131
—
methylene chloride, 1,1,1
-
trichloroethane, chlorobenzene,
o-dichlorobenzene, cresols, cresylic
acid, nitrobenzene, toluene, methyl
ethyl
ketone,
carbon
disulfide,
isobutanol, pyridine,
spent chloro
fluorocarbon solvents
—
provided that
the maximum total weekly usage of these
solvents
(Other
than
the
amounts
that
can be demonstrated not to be discharged
to
wastewater)
divided
by
the
average
weekly
flow
of
wastewater
into
the
headworks
of
the
facility’s
wastewater
treatment
or
pre—treatment
system
does
not exceed 25 parts per million; or
iii)
One
of
the
following
wastes
listed
in
Section 721.132
-
heat exchanger bundle
cleaning sludge from the petroleum
refining
industry
(EPA
Hazardous
Waste
No.
K050);
or
iv)
A
discharged
commercial
chemical
product,
or
chemical
intermediate
listed
in
Section
721.133,
arising
from
de
minimis losses of these materials from
manufacturing operations in which these
materials are used as rawmaterials or
are produced in the manufacturing
process.
For purposes of this
subsection,
“de minimis” losses include
those from normal material handling
operations
(e.g.,
spills from the
unloading or transfer of materials from
bins or other containers,
leaks from
pipes, valves or other devices used to
transfer materials); minor leaks of
process
equipment,
storage
tanks
or
containers;
leaks from well—maintained
pump packings and seals; sample
purgings; relief device discharges;
128—551
82
discharges from safety showers and
rinsing and cleaning of personal safety
equipment; and rinsate from empty
containers or from containers that are
rendered
empty
by
that
rinsing;
or
v)
Wastewater resulting from laboratory
operations containing toxic
(T) wastes
listed in Subpart
D, provided that the
annualized average flow of laboratory
wastewater does not exceed one percent
of total wastewater flow into the
headworks of the facility’s wastewater
treatment or pre—treatment system, or
provided that the wastes combined
annualized average concentration does
not
exceed
one
part
per
million
in
the
headworks of the facility’s wastewater
treatment or pre-treatment facility.
Toxic
(T) wastes used in laboratories
that are demonstrated not to be
discharged to wastewater are not to be
included in this calculation.
b)
A
solid
waste
which
is
not
excluded
from
regulation
under subsection
(a) (1) becomes a hazardous waste when
any
of
the
following
events
occur:
1)
In the case of a waste listed in Subpart
D, when
the waste first meets the listing .description set
forth in Subpart D.
2)
In the case of a mixture of solid waste and one or
more listed hazardous wastes, when a hazardous
waste listed in Subpart D is first added to the
solid waste.
3)
In the case of any other waste (including a waste
mixture), when the waste exhibits any of the
characteristics identified in Subpart
C.
c)
Unless and until it meets the criteria of subsection
(d):
1)
A hazardous waste will remain a hazardous waste.
2)
Specific inclusions and exclusions
A)
Except as otherwise provided in subsection
(c) (2) (B), any solid waste generated from the
treatment,
storage
or disposal of a hazardous
waste, including any sludge,
spill residue,
128—552
83
ash, emission control dust or leachate (but
not including precipitation run—off),
is a
hazardous waste.
(However, materials that
are reclaimed from solid wastes and that are
used beneficially are not solid wastes and
hence are not hazardous wastes under this
provision unless the reclaimed material is
burned for energy recovery or used in a
manner constituting disposal.)
B)
The following solid wastes’ are not hazardous
even though they are generated from the
treatment,
storage or disposal of a hazardous
waste,
unless
they
exhibit
one
or
more
of
the
characteristics
of
hazardous
waste;
i)
Waste pickle liquor sludge generated by
lime
stabilization
of
spent
pickle
liquor from the iron and steel industry
(SIC Codes 331 and 332)
(Standard
Industrial Codes, as defined and
incorporated by reference in 35 Ill.
Adm. Code 720.110 and 720.111).
ii)
Wastes from burning any of the materials
exempted from regulation by Section
721.106(a)(3)(E),
(F),
(G)T
~
d)
Any
solid
waste
described
in
subsection
(c)
is
not
a
hazardous
waste
if
it
meets
the
following
criteria:
1)
In the case of any solid waste,
it does not
exhibit any of the characteristics of hazardous
waste identified in Subpart
C.
(However, wastes
which exhibit a characteristic at the point of
generation may still be sub-lect to the
requirements of
35 Ill. Ada. Code 728. even if
they no longer exhibit a characteristic at the
point of land disposal.)
2)
In the case of a waste which is a listed waste
under Subpart D, contains a waste listed under
Subpart D or is derived frQm a waste listed in
Subpart D,
it also has been excluded from
subsection
(c)
under
35
Ill.
Ada.
Code
720.120
and
720. 122.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section
721.104
Exclusions
128—553
84
a)
Materials which are not solid wastes.
The following
materials are not solid wastes for the purpose of this
Part:
1)
Sewage:
A)
Domestic sewage; and
B)
Any mixture of domestic sewage and other
waste that passes through a sewer system to
publicly—owned
treatment
works
for
treatment.
“Domestic sewage” means untreated sanitary
wastes that pass through a sewer system.
2)
Industrial wastewater discharges that are point
source discharges with NPDES permits issued by the
Agency pursuant to Section 12(f) of the
Environmental Protection Act and 35 Ill.
Adm. Code
309.
BOARD
NOTE:
This
exclusion
applies
only
to
the
actual point source discharge.
It does not
exclude industrial wastewaters while they are
being collected,
stored or treated before
discharge, nor does it exclude sludges that are
generated
by
industrial
wastewater
treatment.
3)
Irrigation return flows.
4)
Source, special nuclear or by—product material as
defined by the Atomic Energy Act of 1954,
as
amended
(42 U.S.C. 2011 et seq.)
5)
Materials subjected to in-situ mining techniques
which are not removed from the ground as part of
the extraction process.
6)
Pulping liquors (i.e., black liquor) that are
reclaimed in a pulping liquor recovery furnace and
then reused in the pulping process, unless
accumulated
speculatively
as
defined
in
Section
721.101(c);
7)
Spent sulfuric acid used to produce virgin
sulfuric acid, unless it is accumulated
speculatively as defined in Section 721.101(c).
8)
Secondary
materials
that
are
reclaimed
and
returned to the original process or processes in
which they were generated where they are reused in
the production process, provided:
128—554
85
A)
Only tank storage is involved, and the entire
process through completion of reclamation is
closed by being entirely connected with pipes
or other comparable enclosed means of
conveyance;
B)
Reclamation does not involve controlled flame
combustion (such as occurs in boilers,
industrial furnaces or incinerators);
C)
The secondary materials are never accumulated
in such tanks for over twelve months without
being reclaimed; and
D)
The reclaimed material is not used to produce
a fuel, or used to produce products that are
used in a manner constituting disposal.
9)
Wood
preserving
wastes.
A)
Spent wood preserving solutions that. have
been used and are reclaimed and reused for
their original intended purpose;
and
B)
Wastewaters from the wood preserving process
that have been reclaimed and are reused to
treat wood.
j~.Qj
When
used as a fuel,
coke and coal tar from the
iron and steel industry that contains or is
produced from decanter tank tar sludge, USEPA
hazardous waste K087.
The process of producing
coke and coal tar from such decanter tank tar
sludge in a coke oven is likewise excluded from
regulation.
b)
Solid wastes which are not hazardous wastes.
The
following solid wastes are not hazardous wastes:
1)
Household
waste,
including
household
waste
that
has been collected, transported,
stored, treated,
disposed, recovered (e.g., refuse—derived fuel)
or
reused.
“Household waste” means any waste
material (including garbage, trash and sanitary
wastes in septic tanks) derived from households
(including single and multiple residences, hotels
and motels,
bunkhouses,
ranger stations, crew
quarters, campgrounds, picnic grounds and day—use
recreation areas).
A resource recovery facility
managing municipal solid waste shall not be deemed
to be treating,
storing,,disposing of or otherwise
128—555
86
managing hazardous wastes for the purposes of
regulation under this Part,
if such facility:
A)
Receives
and
burns
only:
i~
Household waste
(from single and
multiple dwellings,
hotels, motels and
other residential sources) and
ii)
Solid waste from commercial or
industrial
sources
that
does
not
contain
hazardous waste; and
B)
Such facility does not accept hazardous waste
and the owner or operator of such facility
has
established
contractual
requirements
or
other appropriate notification or inspection
procedures to assure that hazardous wastes
are not received at or burned in such
facility.
2)
Solid
wastes
generated
by
any
of
the
following
and
which
are
returned
to
the
soil
as
fertilizers:
A)
The growing and harvesting of agricultural
crops.
B)
The
raising
of
animals,
including
animal
manures.
3)
Mining
overburden
returned
to
the
mine
site.
4)
Fly
ash
waste,
bottom
ash
waste,
slag
waste7
and
flue gas emission control waste generated
primarily from the combustion of coal or other
fossil fuels, except as provided in
35 Ill. Ada.
Code 726.212 for facilities that burn or
process
hazardous waste.
5)
Drilling fluids, produced waters, and other wastes
associated with the exploration, development, or
production of crude oil, natural gas or geothermal
energy.
6)
Chromium wastes:
A)
Wastes which fail the test for the toxicity
characteristic (Section 721.124 and Appendix
B) because chromium is present or are listed
in
Subpart
D
due
to
the
presence
of
chromium,
which do not fail the test for the toxicity
characteristic for any other constituent or
128—556
87
are not listed due to the presence of any
other constituent, and which do not fail the
test for any other characteristic,
if it is
shown by a waste generator or by waste
generators that:
i)
The chromium in ‘the waste is exclusively
(or nearly exclusively) trivalent
chromium; and
ii)
The waste is generated from an
industrial process which uses trivalent
chromium exclusively
(or nearly
exclusively) and the process does not
generate hexavalent chromium; and
iii)
The
waste.
is
typically
and
frequently
managed in non—oxidizing environments.
B)
Specific wastes which meet the standard in
subsections
(b) (6) (A) (i),
(ii) and
(iii)
(so
long as they do not fail the test for the
characteristic
of
EP
toxicity,
and
do
not
fail
the
test
for
any
other
characteristic)
are
i)
Chrome
(blue)
trimmings generated by the
following
subcategories
of
the
leather
tanning and finishing industry; hair
pulp/chrome tan/retan/wet finish; hair
save/chrome tan/retan/wet finish;
retan/wet finish; no beamhouse; through-
the-blue; and shearling.
ii)
Chrome
(blue)
shavings generated by the
following
subcategories
of
the
leather
tanning and finishing industry; hair
pulp/chrome tan/retan/wet finish; hair
save/chrome tan/retan/wet finish;
retan/wet finish; no beamhouse; through-
the-blue; and shearling.
iii) Buffing dust generated by the following
subcategories of the leather tanning and
finishing industry:
hair pulp/chrome
tan/retan/wet finish; hair save/chrome
tan/retan/wet finish; retan/wet finish;
no beamhouse; through—the-blue.
iv)
Sewer screenings generated by the
following
subcategories
‘of
the
leather
tanning and finishing industry:
hair
128—557
88
pulp/chrome tan/retan/wet finish; hair
save/chrome tan/retan/wet finish;
retàn/wet finish; no beamhouse; through-
the-blue; and shearling.
v)
Wastewater treatment sludges generated
by the following subcategories of the
leather tanning and finishing industry:
hair pulp/chrome tan/retan/wet finish;
hair save/chrome tan/retan/wet finish;
retan/wet finish; no beamhouse; through-
the-blue; and shearling.
vi)
Wastewater treatment sludges generated
by the following subcategories of the
leather tanning and finishing industry:
hair pulp/chrome tan/retan/wet finish;
hair save/chrome tan/retan/wet finish;
and through-the-blue.
vii) Waste scrap leather from the leather
tanning industry, the shoe manufacturing
industry, and other leather product
manufacturing industries.
viii)
Wastewater
treatment
sludges
from
the
production
of
titanium
dioxide
pigment
using chromium—bearing ores
by
the
chloride
process.
7)
Solid
waste
from
the
extraction,
beneficiation
and
processing of ores and minerals (including coal~3—~
including phosphate rock and overburden from the
mining of uranium ore), except as provided by 35
Ill.
Ada.
Code
726.212
for
facilities
that
burn
or
process
hazardous
waste.
For
purposes
of
this
subsection, beneficiation of ores and minerals is
restricted to the following activities:
crushing,
grinding, washing, dissolution, crystallization,
filtration,
sorting, sizing, drying,
sintering,
pelletizing, briquetting, calcining to remove
water or carbon dioxide, roasting, autoclaving or
chlorination in preparation for leaching (except
where the roasting or autoclaving or
chlorination) /leaching sequence produces a final
or intermediate product that does not undergo
further beneficiation or processing), gravity
concentration, magnetic separation,
electrostatic
separation,
floatation,
ion exchange, solvent
extraction, electrowinning,
precipitation,
amalgamation, and heap,
dump,
vat tank and in situ
leaching.
For the purposes of this subsection,
128—558
89
solid waste from the processing of ores and
minerals will include~only the following wastes:
A)
Slag from primary copper processing;
B)
Slag from primary lead processing;
C)
Red and brown muds from bauxite refining;
D)
Phosphogypsum from phosphoric acid
production;
E)
Slag from elemental phosphorus production;
F)
Gasifier
ash
from
coal
gasification;
G)
Process
wastewater
from
coal
gasification;
H)
Calcium sulfate wastewater treatment plant
sludge from primary copper processing;
I)
Slag tailings from primary copper processing;
J)
Fluorogypsum
from
hydrofluoric
acid
production;
K)
Process
wastewater
from
hydrofluoric
acid
production;
L)
Air
pollution
control
dust/sludge
from
iron
blast
furnaces;
M)
Iron blast furnace slag;
N)
Treated residue from roasting/leaching of
chrome
ore;
0)
Process wastewater from primary magnesium
processing by the anhydrous process;
P)
Process wastewater from phosphoric acid
production;
Q)
Basic oxygen furnace and cpen hearth furnace
air pollution control dust/sludge from carbon
steel production;
R)
Basic oxygen furnace and open hearth furnace
slag from carbon steel production;
5)
Chloride processing.waste solids from
titanium tetrachloride production;
and,
128—559
90
T)
Slag from primary zinc smelting.
8)
Cement kiln dust waste, except as provided by 35
Ill. Ada. Code 266.212 for facilities that burn or
process hazardous waste.
9)
Solid waste which consists of discarded wood or
wood products which fails the test for the
toxicity characteristic solely for arsenic and
which is not a hazardous waste for any other’
reason or reasons if the waste is generated by
persons who utilize the arsenical—treated wood and
wood products for these materials’ intended end
use.
10)
Petroleum-contaminated
media
and
debris
that
fail
the test for the toxicity characteristic of
Section 721.124
(hazardous waste codes D018
through D043 only)
and are subject to corrective
action regulations under 35 Ill. Ada. Code 731.
11)
Glniected
groundwater
that
that
is
hazardous
only
because it exhibits the toxicity characteristic
(USEPA hazardous waste codes D018 throuah D024
only)_in Section 721.124 that is reinjected
e~
reinfiltratedthrough an underground iniection well
pursuant to exi3tingfree mhase hydrocarbon
recovery operations undertaken at petroleum
refineries,
petroleum marketing terminals—e~
petroleum bulk plants handling crudc pctroleum or
intcrmediate product3 of pctrolcum refining until
March 25,
1991.. petroleum pipelines and petroleum
spill sites until JanuarY 25.
1993.
This
extension applies to recovery operations in
existence, or for which contracts have been
issued
on or before March 25,
1991.
For
groundwater returned through infiltration
galleries from such at petroleum refineries,
marketing terminals and bulk plants,
until October
2,
1991.
New operations involving iniectiQn wells
(beginning after March 25.
1991) will aualify for
this
compliance
date
extension
(until
January
25,
1993) only if:
~j
Operations are performed pursuant to a
written
State
agreement
that
includes
a
provision to assess the groundwater and the
need for further remediation once the free
phase recovery is completed;
and
~j.
A copy of the written agreement has been
128—560
91
submitted to:
Characteristics Section
(OS-333)
USEPA
401 M Street, SW
Washington.
D.C.
20460
~J
Used chlorofluorocarbon
refrigerants
from
totally
enclosed heat transfer eauipment.
including mobile
air
conditioning systems, mobile refrigeration.
and commercial and industrial air conditioning and
refrigeration systems. which use chlorofluoro—
carbons as the heat transfer fluid in a
refrigeration cycle. provided the refriaerant is
reclaimed for further use.
c)
Hazardous wastes which are exempted from certain
regulations.
A
hazardous waste which is generated in a
product
or
raw
material
storage
tank,
a
product
or
raw
material
transport
vehicle
or
vessel,
a
product
or
raw
material
pipeline,
or
in
a
manufacturing
process
unit
or an associated non—waste—treatment manufacturing
unit,
is not subject to regulation under 35 Ill.
Ada.
Code 702,
703,
705 and 722 through 725 and 728 or to
the
notification
requirements
of
Section
3010
of
RCRA
until it exits the unit in which it was generated,
unless the unit is a surface impoundment, or unless the
hazardous waste remains in the unit more than 90 days
after the unit ceases to be operated for manufacturing,
or for storage or transportation of product or raw
materials.
d)
Samples
1)
Except as provided in subsection
(d) (2),
a sample
of solid waste or a sample of water,
soil or air,
which
is
collected
for
the
sole
purpose
of
testing
to determine its characteristics or composition,
is not subject to any requirements of this Part or
35 Ill. Ada. Code 702, 703, 705 and 722 through
728.
The sample qualifies when:
A)
The sample is being transported to a
laboratory for the purpose of testing; or
B)
The sample
is being transported back to the
sample collector after testing; or
C)
The sample
is being stored by the sample
collector before transport to a laboratory
for testing; or
128—561
92
D)
The
sample
is
being
stored
in
a
laboratory
before testing; or
E)
The
sample
is
being
stored
in
a
laboratory
for testing but before it is returned to the
sample collector;
or
F)
The sample is being stored temporarily in the
laboratory after testing for a specific
purpose
(for example, until conclusion of a
court case or enforcement action where
further testing of the sample may be
necessary).
2)
In order to qualify for the exemption in
subsection
(d) (1) (A) and
(B), a sample collector
shipping samples to a laboratory and a laboratory
returning samples to a sample collector must:
A)
Comply with U.S. Department of Transportation
(DOT), U.S. Postal Service (USPS)
or any
other applicable shipping requirements; or
B)
Comply with the following requirements if the
sample collector determines that DOT, USPS or
other shipping requirements do not apply to
the shipment of the sample:
i)
Assure that the following information
accompanies the sample:
The sample
collector’s name, mailing address and
telephone number; the laboratory’s name,
mailing address and telephone number;
the quantity of the sample; the date of
the shipment; and a description of the
sample.
ii)
Package the sample so that it does not
-leak,
spill or vaporize from its
packaging.
3)
This exemption does not apply if the laboratory
determines that the waste is hazardous but the
laboratory is no longer meeting any of the
conditions stated in subsection
(d) (1).
e)
Treatability study samples.
1)
Except as is provided in subsection
(e)(2),
persons who generate or collect samples for the
purpose of conducting treatability studies, as
defined in 35 Ill. Ada. Code 720.110, are not
128—562
93
subject to any requirement of 35
Ill. Ada. Code
721 through 723 or to the notification
requirements of Section 3010 of the Resource
Conservation and Recovery Act.
Nor are such
samples included in the quantity determinations of
Section 721.105 and 35 Ill. Ada. Code 722.134(d)
when:
A)
The sample is being collected and prepared
for transportation by the generator or sample
collector;
or,
B)
The sample is being accumulated or stored by
the generator or sample collector prior to
transportation to a laboratory or testing
facility;
or
C)
The sample is being transported to the
laboratory or testing facility for the
purpose of conducting a treatability study.
2)
The exemption in subsection
(e) (1)
is applicable
to samples of hazardous waste being collected and
shipped for the purpose of conducting treatability
studies’
provided
that:
A)
The
generator
or
sample
collector
uses
(in
“treatability studies”) no more than 1000 kg
of any non—acute hazardous waste,
1 kg of
acute hazardous waste or 250 kg of soils,
water
or
debris
contaminated
with
acute
hazardous waste for each process being
evaluated for each generated wastestream; and
B)
The mass of each shipment does not exceed
1000 kg of non—acute hazardous waste,
1 kg of
acute hazardous waste or 250 kg of soils,
water or debris contaminated with acute
hazardous waste; and
C)
The sample must be packaged so that it does
not leak, spill or vaporize from its
packaging during shipment and the
requirements of subsections
(i) or
(ii) are
met.
i)
The transportation of each sample
shipment complies with US.
Department
of
Transportation
(DOT),
U.S.
Postal
Service
(USPS)
or any other applicable
shipping requirements; or
128—5 63
94
ii)
If the DOT, USPS or other shipping
requirements do not apply to the
shipment of the sample, the following
information must accompany the sample:
The name, mailing address and telephone
number
of the originator of the sample;
the name,
address and telephone
number
of the facility that will perform the
treatability study; the quantity of the
sample; the date of the shipment;
and, a
description of the sample,
including its
USEPA hazardous waste number.
D)
The sample is shipped to
a laboratory or
testing facility which is exempt under
subsection
(f)
or has an appropriate RCRA
permit or interim status.
E)
The
generator
or
sample
collector
maintains
the following records for a period ending
3
years after completion of the treatability
study:
i)
Copies of the shipping documents;
ii)
A
copy
of
the
contract
with
the
facility
conducting the treatabili.ty study;
iii) Documentation showing:
The amount of
waste shipped under this exemption; the
name, address and USEPA identification
number of the laboratory or testing
facility that received the waste; the
date the shipment was made; and, whether
or not unused samples and residues were
returned to the generator.
F)
The generator reports the information
required
in
subsection
(e)
(2)
(E) (iii)
in
its
report under 35 Ill. Ada. Code 722.141.
3)
The Agency may grant requests, on a case—by-case
basis,
for quantity limits in excess of those
specified in subsection
(e) (2) (A), for up to an
additional 500 kg of any non-acute hazardous
waste,
1 kg of acute hazardous waste and 250 kg of
soils, water or debris contaminated with acute
hazardous waste, to conduct further treatability
study evaluation when:
There has been an
equipment or mechanical failure during the conduct
of the treatability study; there is need to verify
the results of a previously conducted treatability
128—564
95
study; there is a need to study and analyze
alternative techniques within a previously
evaluated treatment process;
or, there is a need
to
do
further
evaluation
of
an
ongoing
treatability study to determine final
specifications for treatment.
The additional
quantities allowed are subject to all the
provisions in subsections
(e) (1) and
(e) (2) (3)
through
(F).
The generator or sample collector
must apply to the Agency and provide in writing
the following information:
A)
The reason why the generator or sample
collector requires additional quantity of
sample for the treatability study evaluation
and the additional quantity needed;
B)
Documentation accounting for all samples of
hazardous waste from the wastestream which
have been sent for or undergone treatability
studies,
including the date each previous
sample was shipped, the quantity of each
previous shipment, the laboratory or testing
facility to which it was shipped, what
treatability study processes were conducted
on each sample shipped, and the available
results of each treatability study;
C)
A description of the technical modifications
or change in specifications which will be
evaluated
and
the
expected
results;
D)
If such further study is being required due
to equipment or mechanical failure, the
applicant
must
include
information
regarding
the
reason
for
the
failure
or
breakdown
and
also
include
what
procedures
or
equipment
have been made to protect against further
breakdowns;
and,
E)
Such other information as the Agency
determines is necessary.
4)
Final
Agency
determinations
pursuant
to
this
subsection may be appealed to the Board.
f)
Samples
undergoing
treatability
studies
at
laboratories
or testing facilities.
Samples undergoing treatability
studies and the laboratory or testing facility
conducting such treatability studies
(to the extent
such facilities are not otherwise subject to RCRA
requirements)
are
not
subject
to
any requirement of
128—565
96
this
Part,
or
of
35
Ill.
Ada.
Code
702,
703,
705,
722
through 726, and 728, or to the notification
requirements of Section 3010 of the Resource
Conservation and Redovery Act, provided that the
requirements of subsections
(f) (1) through
(f) (11) are
met.
A mobile treatment unit may qualify as a testing
facility subject to subsections
(f) (1) through
(f) (11).
Where a
group of mobile treatment units are located at
the same site, the limitations specified in subsections
(f) (1) through
(f) (11) apply to the entire group of
mobile treatment units collectively as if the group
were one mobile treatment unit.
1)
No less than 45 days before con’ducting
treatability studies, the facility notifies the
Agency
in
writing
that
it intends to conduct
treatability
studies
under
this
subsection.
2)
The
laboratory
or
testing
facility
conducting
the
treatability study has a USEPA identification
number.
3)
No more than a total of 250 kg of “as received”
hazardous waste
is subjected to initiation of
treatability studies in any single day.
“As
received” waste refers to the waste as received in
the shipment from the generator or sample
collector.
4)
The
quantity
of
“as
received”
hazardous
waste
stored at the facility for the purpose of
evaluation in treatability studies does not exceed
1000 kg, the total of which can include 500 kg of
soils, water or debris contaminated with acute
hazardous waste or
1 kg of acute hazardous waste.
This
quantity
limitation
does
not
include:
A)
Treatability study residues;
and,
B)
Treatment materials (including nonhazardous
solid waste)
added to “as received” hazardous
waste.
5)
No more than 90 days have elapsed since the
treatability study for the sample was completed,
or no more than one year has elapsed since the
generator or sample collector shipped the sample
to the laboratory or testing facility, whichever
date first occurs.
6)
The treatability study does not involve the
placement
of
hazardous
waste
on
the
land
or
open
128—566
97
burning of hazardous waste.
7)
The facility maintains records for 3 years
following
completion
of
each
study
that
show
compliance with the treatment rate limits and the
storage time and quantity limits.
The following
specific information must be included for each
treatability study conducted:
A)
The name,
address and USEPA identification
number
of the generator or sample collector
of
each
waste
sample;
B)
The date the shipment was received;
C)
The
quantity
of
waste
accepted;
D)
The quantity of “as received” waste in
storage each day;
E)
The
date
the
treatment
study
was
initiated
and the amount of “as received” waste
introduced
to
treatment
each
day;
F)
The
‘date
the
treatability
study
was
concluded;
G)
The date any unused sample or residues
generated from the treatability study were
returned to the generator or sample collector
or, if sent to a designated facility, the
name of the facility and the USEPA
identification
number.
8)
The
facility
keeps,
on—site,
a
copy
of
the
treatability study contract and all shipping
papers associated with the transport of
treatability study samples to and from the
facility for a period ending
3 years from the
completion date of each treatability study.
9)
The facility prepares and submits a report to the
Agency
by
March
15
of
each
year
that
estimates
the
number
of studies and the amount of waste expected
to be used in treatability studies during the
current year, and includes the following
information for the previous calendar year:
A)
The name,
address and USEPA identification
number of the facility conducting the
treatability
studies;
128—567
98
B)
The types
(by process)
of treatability
studies conducted;
C)
The names and addresses of persons for whom
studies have been conducted (including their
USEPA identification numbers);
D)
The total quantity of waste in storage each
day;
E)
The
quantity
and
types
of
waste
subjected
to
treatability studies;
F)
When each treatability study was conducted;
G)
The final disposition of residues and unused
sample
from
each
treatability
study;
10)
The facility determines whether any unused sample
or residues generated by the treatability study
are hazardous waste under Section 721.103 and,
if
so,
are
subject’
to
35
Ill.
Ada.
Code
702,
703
and
721 through 728, unless the residues and unused
samples are returned to the sample originator
under the subsection
(e). exemption.
11)
The facility notifies the Agency by letter when
the facility is no longer planning to conduct any
treatability studies at the site.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
Section 721.106
Requirements for Recyclable Materials
a)
Recyclable materials:
1)
Hazardous wastes that are recycled are subject to
the requirements for generators,
transporters and
storage facilities of subsections
(b)
and
(c),
except for the materials listed in subsections
(a) (2) and
(a) (3).
Hazardous wastes that are
recycled will be known as “recyclable materials”.
2)
The following recyclable materials are not subject
to the requirements of this Section but are
regulated under 35 Ill.
Ada.
Code 726.Subparts C
through Gfl and all applicable provisions in 35
Ill. Ada. Code 702, 703 and 705.
A)
Recyclable materials used in a manner
constituting disposal
(35 Ill. Adm. Code
128—568
99
726.Subpart C);
B)
Hazardous
wastes
burned
for
energy
recovery
in boilers and industrial furnaces that are
not regulated under 35 Ill. Ada. Code 724 or
725.Subpart 0
(35 Ill. Ada. Code 726.Subpart
DII.)
C)
Used oil that exhibits one or more of the
characteristics of hazardous waste and is
burned for energy recovery in boilers or
industrial furnaces that are not regulated
under 35 Ill. Ada. Code 724 or 725.Subpart 0.
(35 Ill.
Ada. Code 726.Subpart E);
D)
Recyclable materials ~fromwhich precious
metals are reclaimed (35 Ill. Adm. Code
726.Subpart F);
E)
Spent lead-acid’batteries that are being
reclaimed
(35 Ill. Ada. Code 726.Subpart G).
3)
The following recyclable materials are not subject
to regulation under 35
Ill.
Ada. Code 722 through
726, 728,
or 702, 703 or 705 and are not subject
to the notification requirements of Section 3010
of the Resource Conservation and Recovery Act:
A)
Industrial ethyl alcohol that is reclaimed
except that, unless provided otherwise in an
international agreement as specified in 35
Ill.
Adm. Code 722.158:
1)
A person initiating a shipment for
reclamation in a foreign country, and
any intermediary arranging for the
shipment, shall comply with the
requirements applicable to a primary
exporter
in
35
Ill.
Ada.
Code
722.153,
722.156(a) (1) through .(a)(4),
(a)(6)
and
(b), and 722.157, shall export such
materials only upon consent of the
receiving country and in conformance
with the USEPA Acknowledgement of
Consent as defined in 35 Ill. Ada. Code
722.Subpart E, and shall provide a copy
of the USEPA Acknowledgement of Consent
to the shipment to the transporter
transporting the shipment for export;
ii)
Transporters transporting a shipment for
export shall not accept a shipment if
128—569
100
the transporter knows the shipment does
riot conform to the USEPA Acknowledgement
of Consent, shall ensure that.a copy of
the USEPA Acknowledgement of Consent
accompanies the shipment and shall
ensure that it is delivered to the
facility designated by the person
initiating the shipment.
B)
Used batteries (or used battery cells)
returned to a battery manufacturer for
regeneration;
C)
Used oil that exhibits one or more of the
characteristics of hazardous waste but is
recycled in some other manner than being
burned for energy recovery;
D)
Scrap metal;
E)
Fuels produced from the refining of oil—
bearing hazardous wastes along with normal
process streams at a petroleum refining
facility if such wastes result from normal
petroleum refining, production and
transportation practices;
F)
Oil reclaimed from hazardous waste resulting
from normal petroluem refining, production
and transportation practices, which oil is to
be refined along with normal process streams
at a petroleum refining facility;
G)
Coke and coal tar from
the
iron and steel
industry that contains UCEPA hazardous waste
number K087
(dccanter tank tar sludge from
coking operations)
(Cection 721.132) from thc
iron and stcel production proce3s;
H)
Petroleum refining wastes.
i)
Hazardous waste fuel produced from oil—
bearing hazardous wastes from petroleum
refining, production or transportation
practices,
or produced from oil
reclaimed from such hazardous wastes,
where such hazardous wastes are
reintroduced into a process that does
not use distillation or does not produce
products from crude oil so long as the
resulting fuel meets the used oil
specification under 35 Ill. Ada. Code
128—570
101
726.140(e) and so long as no other
hazardous wastes are used to produce the
hazardous waste fuel;
ii)
Hazardous waste fuel produced from oil—
bearing
hazardous
waste
from
petroleum
refining production and transportation
practices, where such hazardous wastes
are reintroduced into a refining process
after a point at which contaminants are
removed, so long as the fuel meets the
used oil fuel specification under 35
Ill. Ada. Code 726.140(e);
and
iii) Oil reclaimed from oil-bearing hazardous
wastes from petroleum refining,
production
and
transportation
practices,
which
reclaimed
oil
is
burned
as
a
fuel
without
reintroduction
to
a
refining
process,
so
long
as
the
reclaimed
oil
meets
the
used
oil
fuel
specification
under
35
Ill.
Ada.
Code
726.140(e);
and
~fl)
Petroleum
coke
produced
from
petroleum
refinery
hazardous
wastes
containing
oil
at
the same facility at which such wastes were
generated, unless the resulting coke product
exceeds one or more of the characteristics of
hazardous waste in Subpart C.
b)
Generators
and
transporters
of
recyclable
materials
are
subject to the applicable requirements of 35 Ill. Ada.
Code
722
and
723
and
the
notification
requirements
under
Section
3010
of
the
Resource
Conservation
and
Recovery
Act,
except
as
provided
in
subsection
(a).
C)
Storage
and
recycling:
1)
Owners or operators of facilities that store
recyclable materials before they are recycled are
regulated under all applicable provisions of 35
Ill.
Ada.
Code
724.Subparts
A
through
L,
AA
and
BB
and 725.Subparts A through L, AA and BB,
726, 728,
702,
703 and 705 and tk~enotification requirement
under Section 3010 of the Resource Conservation
and Recovery Act, except as provided in subsection
(a).
(The recycling process itself
is exempt from
regulation, except as provided in subsection
(d).)
2)
Owners
or
operators
of
facilities
that
recycle
recyclable materials.without storing them before
they are recycled are subject to the following
128—571
102
requirements,
except
as
provided
in
subsection
(a).
A)
Notification requirements under Section 3010
of the Resource Conservation and Recovery
Act.
B)
35
Ill.
Ada.
Code
725.171
and
725.172
(dealing with the use of the manifest and
manifest discrepancies)
C)
Subsection
(d).
d)
Owners or operators of facilities required to have a
RCRA
permit pursuant to 35 Ill. Ada. Code 703 with
hazardous waste management units which recycle
hazardous wastes are subject to 35 Ill. Ada. Code
724.Subpart AA and BB and 725.Subpart AA and BB.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
SUBPART C:
CHARACTERISTICS OF HAZARDOUS WASTE
Section
721.120
General
a)
A solid waste,
as defined in Section 721.102, which is
not excluded from regulation as a hazardous waste under
Section
721.104(b),
is a hazardous waste if it exhibits
any of the characteristics identified in this Subpart.
BOARD
NOTE:
35 Ill. Ada. Code 722.111 sets forth the
generator’s responsibility to determine whether the
generator’s waste exhibits one or more characteristics
identified in this Subpart.
b)
A hazardous waste which is identified by a
characteristic in this Subpart is assigned every USEPA
Hazardous Waste’ Number which is applicable as set forth
in this Subpart.
This number must be used in complying
with the notification requirements of
Sectio.n 3Q10 of
the Resource Conservation and Recovery Act and all
applicable recordkeeping and reporting requirements
under 35 Ill. Ada. Code 702,
703, 722 through ~-2-52~
and 728.
c)
For purposes of this Subpart,
a sample obtained using
any of the applicable sampling methods specified in
Appendix A is a representative sample within the
meaning
of
35
Ill.
Ada.
Code
720.
BOARD
NOTE:
Since
the
Appendix A sampling methods are
128—572
103
not being formally adopted, a person who desires to
employ an alternative sampling method is not required
to
demonstrate
the
equivalency
of
the person’s method
under the procedures set forth. in 35
Ill.
Adm. Code
720.121.
(Source:
Amended at
16 Ill. Reg.
,
effective
)
Section, 721.131
Hazardous Wastes From Nonspecific Sources
a)
The following solid wastes are listed hazardous wastes
from non—specific sources unless they are excluded
under 35 Ill. Adm. Code 720.120 and 720.122 and listed
in
Appendix
I.
EPA
Industry and Hazardous Waste
Haz-
Hazardous
ard
Waste
No.
Code
FOOl
The following spent halogenated
(T)
solvents used in degreasing:
tetra—
chloroethylene, trichloroethylene,
methylene
chloride,
1,1,
1-trichloro-
ethane, carbon tetrachloride and
chlorinated fluorocarbons; all spent
solvent mixtures and blends used in
degreasing containing,
before use,
a
total
of
ten
percent
or
more
(by
volume)
of
one
or
more
of
the
above
halogenated
solvents
or those solvents
listed
in
F002,
F004
or
F005;
and
still
bottoms from the recovery of these
spent
solvents
and
spent
solvent
mixtures.
F002
The following spent halogenated
(T)
solvents:
tetrachloroethylene,
aethy-lene chloride, trichloroethylene,
1, 1, 1—trichloroethane, chlorobenzene,
1,1,2-trichloro—1, 2, 2—trifluoroethane,
orthodichlorobenzene, trichloro—
fluoromethane and 1, 1,2—trichloro—
ethane; all spent solvent mixtures and
blends containing,
before use, a total
of
ten
percent
or
more
(by
volume)
of
one or more of the above halogenated
solvents or those solvents listed in
FOOl,
F004
or
F005;
and
still
bottoms
from the recovery of these spent
solvents and spent solvent mixtures.
128—5 73
104
F003
The following spent non-halogenated
(I)
solvents:
xylene, acetone, ethyl
acetate, ethyl benzene, ethyl ether,
methyl
isobutyl
ketone,
n-butyl
alcohol, cyclohexanone and methanol;
all spent solvent mixtures and blends
containing, before use, only the above
spent
non—halogenated
solvents;
and
all
spent solvent mixtures and blends
containing, before use, one or more of
the above non—halogenated solvents and
a total of ten percent or more (by
volume)
of
one
or
more
of
those
solvents listed in FOOl, F002,
F004 or
F005; and still bottoms from the
recovery of these spent solvents and
spent solvent mixtures.
F004
The following spent non—halogenated
(T)
solvents:
cresols and cresylic acid
and nitrobenzene; all spent solvent
mixtures and blends containing, before
use, a total of ten percent or more (by
volume) of one or more of the above
non—halogenated solvents or those
solvents listed in FOOl, FOO2 or F005;
and still bottoms from the recovery of
these spent solvents and spent solvent
mixtures.
F005
The following spent non-halogenated
(I,
solvents:
toluene, methyl ethyl
T)
ketone,
carbon disulfide,
isobutanol,
pyridine, benzene, 2—ethoxyethanol and
2—nitropropane; all spent solvent
mixtures and blends, containing,
before
use, a total of ten percent or more
(by
volume) of one or more of the above
non—halogenated solvents or those
solvents listed in FOOl, F002 or F004;
and still bottoms from the recovery of
these spent solvents and spent solvent
mixtures.
F006
Wastewater
treatment
sludges
from
(T)
electroplating operations except from
the following processes:
(1)
sulfuric
acid anodizing of’ aluminum;
(2) tin
plating on carbon steel;
(3)
zinc
plating (segregated basis)
on carbon
steel;
(4) aluminum or zinc—aluminum
plating
on carbon steel;
(5)
128—574
105
cleaning/stripping associated with tin,
zinc
and
aluminum
plating
on
carbon
steel;
and
(6) chemical etching and
milling
of
aluminum.
F019
See Below
FOOl
Spent
cyanide
plating
bath
solutions
(R,
from
electroplating
operations.
T)
FOO8
Plating bath residues from the bottom
(R,
of
plating
baths
from electroplating
T)
operations where cyanides are used in
the process.
F009
Spent stripping and cleaning bath
(R,
solutions
from
electroplating
T)
operations where cyanides are used in
the
process.
F010
Quenching bath residues from oil baths
(R,
from metal heat treating operations
T)
where cyanides are used in the process.
FOll
Spent
cyanide
solutions
from
salt
bath
(R,
pot cleaning from metal heat treating
T~
operations.
F012
Quenching
wastewater
treatment
sludges
(T)
from
metal
heat
treating
operations
where
cyanides
are used in the process.
F019
Wastewater
treatment
sludges
from
the
(T)
chemical
conversion
coating
of
aluminum
except from zirconium phosphating in
aluminum can washing when such
phosphating is an
exclusive
conversion
coating process.
F020
Wastes
(except wastewater and spent
(H)
carbon from hydrogen chloride
purification)
from the production or
manufacturing use
(as a reactant,
chemical intermediate or component in a
formulating process) of tn— or tetra—
chlorophenol, or of intermediates used
to produce their pesticide derivatives.
(This listing does not include wastes
from the production of hexachlorophene
from highly purified 2,4,5-trichloro-
phenol.
128—575
106
F021
Wastes
(except
wastewater
and
spent
(H)
carbon from hydrogen chloride
purification) from the production or
manufacturing use
(as a reactant,
chemical intermediate or component in
a
formulating process) of pentachloro—
phenol, or of intermediates used to
produce its derivatives.
F022
Wastes
(except wastewater and spent
(H)
carbon from hydrogen chloride
purification)
from the manufacturing
use
(as a reactant, chemical
intermediate or component in a
formulating process)
of tetra-, penta—
or
hexachlorobenzenes
under
alkaline
conditions.
FO23
Wastes (except wastewater and spent
(H)
carbon from hydrogen chloride
purification) from the production of
materials on equipment previously used
for the production or manufacturing use
(as a reactant, chemical intermediate
or-component in a formulating process)
of
tn-
and
tetrachlorophenols.
(This
listing does not include wastes from
equipment used only for the production
or use of hexachiorophene from highly
purified 2,4,5- trichlorophenol.
F024
Process wastes including but not
(T)
limited
to,
distillation
residues,
heavy ends, tars, and reactor cleanout
wastes, from the production of certain
chlorinated aliphatic hydrocarbons by
free radical catalyzed processes.
These chlorinated aliphatic
hydracarbons are those having carbon
chain lengths ranging from one to and
including five, with varying amounts
and positions of chlorina substitution.
(This listing does not include
wastewaters, wastewater treatment
sludges, spent catalysts and wastes
listed in this Section or Section
721.132.)
FO25
Condensed light ends,
spent filters and
(T)
filter aids,
and spent desicant wastes
from the production of certain
chlorinated
aliphatic
hydrocarbons
by
128—57 6
107
free radical catalyzed processes.
These
chlorinated
aliphatic
hydrocarbons are those having carbon
chain lengths ranging from one to and
including five, with varying amounts
and positions of chlorine substitution.
F026
Wastes
(except
wastewater
and
spent
(H)
carbon from hydrogen chloride
purification) from the production of
materials on equipment previously used
for the manufacturing use (as a
reactant, chemical intermediate or
component in a formulating process)
of
tetra—,
penta—
or
hexachlorobenzene
under
alkaline
conditions.
F027
Discarded unused formulations
(H)
containing tn—, tetra— or pentachloro—
phenol or discarded unused formulations
containing
compounds
derived
from
these
chlorophenols.
(This listing does not
include formulations containing -hexa—
chlorophene synthesized from
prepurified 2,4,5-tnichlorophenol as
the sole component).
F028
Residues resulting from the
(T)
incineration or thermal treatment of
soil
contaminated
with
hazardous
waste
numbers FO2O,
FO21, F022,
FO23,
F026
and
FO27.
FO32
Wastewaters,
process residuals,
(T)
preservative
drippage
and
spent
formulations from wood preserving
processes generated at plants that
currently use or have previously used
chlorophenolic formulations (except
potentially cross—contaminated wastes
that have had the F032 waste code
deleted in accordance with Section
721.135 and where the generator does
not resume or initiate use of chloro—
phenolic formulations).
This listing
does not include KOOl bottom sediment
sludge from the treatment of wastewater
from wood preserving processes that use
creosote or pentachlorophenol.
BOARD
NOTE:
The
listing
of
wastewaters
that have not come into contact with
128—57 7
108
process contaminants is stayed
administratively.
The listing for
plants that have previously used
chlorophenolic formulations is
adainistratively stayed whenever these
wastes are covered by the F034 or F035
listings.
These stays will remain in
effect until further administrative
action is taken.
Furthermore, the F032
listing is administratively stayed with
respect to the process area receiving
drippage of these wastes provided
persons desiring to continue operating
notify USEPA by August
6, 1991,
of
their intent to upgrade or install drip
pads, and by November 6,
1991, provide
evidence to USEPA that they have
adequate financing to pay for drip pad
upgrades or installation, as provided
in the administrative stay.
The stay
of listings will remain in effect until
February 6,
1992,
for existing drip
pads, and until May 6,
1992,
for new
drip pads.
FO34
Wastewaters, process residuals,
(T)
preservative drippage and spent
formulations from wood preserving
processes
generated
at plants that use
creosote formulations.
This listing
does not include KOO1 bottom sediment
sludge from the treatment of wastewater
from wood preserving processes that use
creosote or pentachlorophenol.
BOARD
NOTE:
The listing of wastewaters
that have not come into contact with
process contaminants is stayed
admin-istratively.
These stays will
remain
in effect until further
administrative action is taken.
Furthermore, the F034 and FO35 listings
are administratively stayed with
respect to the process area receiving
dnippage of these wastes provided that,
by November 6,
1991,
persons desiring
to continue operating notify the Agency
of their intent to upgrade or install
drip pads, and provide evidence to the
Agency that they have adequate
financing to pay for drip pad upgrades
or installation,
as provided in the
128—578
109
administrative stay.
The stay of
listings will remain in effect until
February
6,
1992,
for existing drip
pads,
and until May 6, 1992, .for new
drip pads.
FO35
Wastewaters,
process
residuals,
(T)
preservative drippage and spent
formulations
from
wood
preserving
processes generated at plants that use
inorganic preservatives containing
arsenic or chromium.
This listing does
not include KOOl bottom sediment sludge
from the treatment of wastewater from
wood preserving processes that use
creosote or pentachiorophenol.
BOARD
NOTE:
The
listing
of
wastewaters
that have not come into contact with
process contaminants is stayed
administratively.
These stays will
remain in effect until further
administrative action is taken.
Furthermore, the F034 and F035 listings
are administratively stayed with
respect to the process area receiving
drippage of these wastes provided that,
by November 6,
1991,
persons desiring
to continue operating notify the Agency
of
their
intent
to
upgrade
or
install
drip pads,
and provide evidence to the
Agency that they have adequate
financing to pay for drip pad upgrades
or installation, as provided in the
administrative stay.
The stay of
listings will remain in effect until
February 6,
1992,
for existing drip
pads, and until May 6,
1992,
for new
drip .pads.
F037
Petroleum
refinery
primary
oil/water/
(T)
solids separation sludge
--
Any sludge
generated from the gravitational
separation of oil/water/solids during
the storage or treatment of process
wastewaters and oily cooling
wastewaters from petroleum refineries.
Such sludges include, but are not
limited to, those generated in:
oil/
water/solids separators; tanks and
impoundments; ditches and other
conveyances; suaps; and stormwater
units receiving dry, weather flow.
128—579
110
Sludges generated in stormwater
units
that do not receive dry weather flow,
sludges aenerated from non-contact
once-through cooling waters segreaated
for treatment from other process or
oily cooling waters. sludges generated
in aggressive biological treatment
units as defined in subsection
(b) (2)
(including sludges generated in one or
more additional units after wastewaters
have been treated in aggressive
biological treatment units)
and K051
wastes are not included in this
listing.
F038
Petroleum refinery secondary
(T)
(emulsified)
oil/water/solids
separation sludge
——
Any
sludge or
float generated from the physical or
chemical separation of oil/water/solids
in process wastewaters and oily cooling
wastewaters from petroleum refineries.
Such wastes include, but are not
limited to, all sludges and floats
generated in:
induced air floatation
(IAF)
units, tanks and impoundments,
and all sludges generated in DAF units.
Sludges generated in storawater units
that do not receive dry weather flow,
sludges
aenerated
from non—contact
once—through cooling waters segregated
for treatment from other process or
oily cooling waters~sludges and floats
generated in aggressive biological
treatment units as defined in
subsection
(b) (2)
(including sludges
and floats generated in one or more
additional units after wastewaters have
been treated in aggressive biological
treatment units),
F037, KO48 and K051
wastes are not included in this
listing.
FO39
Leachate (liauids which have percolated
(T)
through land disposed wastes) resulting
from the treatment,
storage or disposal
of more than one restricted wastee
cla3sifled by more than one wastc code
classified as hazardous under Subpart
D, or from a mixture of wastes
classified undcr Cubparts C and—D.
(Leachate resulting from the
128—580
111
m~ne~ement~djsp~i,
of one or more of
the
following
USEPA
hazardous
wastes
and
no
other
hazardous
wastes
retains
its USEPA hazardous waste
oodc(s)riumber(s):
F020,
F021, F022,
r023,
F026, F027 or F028.)
BOARD
NOTE:
The
primary
hazardous
properties
of
these
materials have been indicated by the letters T
(Toxicity), R (Reactivity),
I
(Ignitability), and.C
(Corrosivity).
The letter H indicates Acute Hazardous
Waste.
b)
Listing
specific
definitions.
1)
For
the
purpose
of
the
F037
and
FO38
listings,
oil/water/solids isdefined as oil or water or
solids.
2)
For the purposes of the F037 and F038
listings:
A)
Aggressive biological treatment units are
defined
as
units
which
employ
one
of
the
following
four
treatment
methods:
activated
sludge;
trickling
filter;
rotating
biological
contactor
for
the
continuous
accelerated
biological
oxidation
of
wastewaters;
or,
high—rate aeration.
High—rate aeration is a
system of surface impoundments or tanks,
in
which intense mechanical aeration is used to
completely mix the wastes, enhance biological
activity,
and:
i)
The units employ
a minimum of
6
horsepower per million gallons of
treatment
volume;
and
either
ii)
The hydraulic retention time of the unit
Ls no longer than 5 days; or
iii) The hydraulic retention time is no
longer than 30 days and the unit does
not generate a sludge that is a
hazardous waste by the toxicity
characteristic.
B)
Generators and treatment, storage or disposal
(TSD)
facilities have the burden of proving
that their sludges are exempt from listing as
FO37 or FO38 wastes under this definition.
Generators and TSD facilities shall maintain,
in their operating or other on site records,
128—581
112
documents and data sufficient to prove that:
i)
The unit is an aggressive biological
treatment unit as defined in this
subsection; and
ii)
The sludges sought to be exempted from
F037 or F038 were actually generated in
the aggressive biological treatment
unit.
3)
Time of generation.
For the purposes of:
A)
The F037 listing, sludges are considered to
be generated at the moment of deposition in
the unit, where deposition is defined as at
least a temporary cessation of lateral
particle movement.
B)
The
F038
listing:
i)
Sludges are considered to be generated
at the moment of deposition in the unit,
where deposition is defined as at least
a temporary cessation of lateral
particle movement; and
ii)
Floats are considered to be generated at
the moment they are formed in the top of
the
unit.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section 721.132
Hazardous Waste from Specific Sources
The following solid wastes are listed hazardous wastes from
specific sources unless they are excluded under 35 Ill. Adm. Code
720.120
and
720.122
and
listed
in
Appendix
I.
EPA
Hazardous
Hazard
Waste No.
Industry and Hazardous Waste
Code
Wood Preservation:
1001
Bottom sediment sludge from the treatment of
(T)
wastewaters
from
wood
preserving
processes
that use creosote and/or pentachlorophenol.
128—582
113
Inorganic Pigments:
1002
Wastewater treatment sludge from the
(T)
production of chrome yellow and orange
pigments.
K003
Wastewater treatment sludge from the
(T)
production of molybdate orange pigments.
1004
Wastewater
treatment
sludge
from
the
(T)
production
of
zinc
yellow
pigments.
K005
Wastewater
treatment
sludge
from
the
(T)
production of chrome green pigments.
1006
Wastewater
treatment
sludge
from
the
(T)
production
of
chrome
oxide
green
pigments
(anhydrous and hydrated).
1007
Wastewater treatment sludge from the
(T)
production
of
iron
blue
pigments.
1008
Oven
residue
from
the
production
of
chrome
(T)
oxide
green
pigments.
Organic Chemicals:
K009
Distillation bottoms from the production of
(T)
acetaldehyde from ethylene.
1010
Distillation side cuts from the production
(T)
of acetaldehyde from ethylene.
1011
Bottom stream from the wastewater stripper
(R,T)
in the production of acrylonitrile.
1013
Bottom stream from the acetronitrile column
(T)
in the production of acrylonitrile.
1014
Bottoms from the acetontrile purification
(T)
column in the production of acrylonitrile.
1015
Still bottoms from the distillation of
(T)
benzyl chloride.
1016
Heavy
ends
or
distillation
residues
from
the
(T)
production
of
carbon
tetrachloride.
K017
Heavy
ends (still bottoms) from the
(T)
purification column in the production of
epichlorohydrin.
128—583
114
1018
Heavy ends from the fractionation column in
(T)
ethyl
chloride
production.
1019
Heavy ends from the distillation of ethylene
(T)
dichioride in ethylene dichloride
production.
K020
Heavy ends from the distillation of vinyl
(T)
chloride in vinyl chloride monomer
production.
1021
Aqueous spent antimony catalyst waste from
(T)
fluoromethanes production.
1022
Distillation bottom tars from the production
(T)
of
phenol/acetone
from
cumene.
1023
Distillation light ends from the production
(T)
of phthalic anhydride from naphthalene.
1024
Distillation bottoms from the production of
(T)
phthalic anhydride from naphthalene.
1093
Distillation light ends from the production
(T)
of phthalic’anhydride from ortho-xylene.
1094
Distillation bottoms from the production of
(T)
phthalic anhydride from ortho-xylene.
1025
Distillation
bottoms
from
the production of
(T)
nitrobenzene
by
the
nitration
of
benzene.
1026
Stripping still tails from the production of
(T)
methyl
ethyl
pyridines.
1027
Centrifuge
and
distillation
residues
from
(R,T)
toluene diisocyanate production.
1028
Spent catalyst- from the hydrochiorinator
(T)
reactor in the production of 1,1,1-tn-
chloroethane.
1029
Waste from the product stream stripper in
(T)
the production of 1,1,1-trichioroethane.
K095
Distillation bottoms from the production of
(T)
1,1,
1-tnichloroethane.
1096
Heavy ends from the heavy ends column from
(T)
the
production
of
1,1,
1-trichloroethane.
128—584
115
1030
Column
bottoms
or
heavy
ends
from
the
(T)
combined production of tnichloroethylene and
perchioroethylene.
1083
Distillation bottoms from aniline
(T)
production.
K103
Process residues from aniline extraction
(T)
from the production of aniline.
K104
Combined wastewater streams generated from
(T)
nitrobenzerie/aniline production.
1085
Distillation or fractionation column bottoms
(T)
from
the
production
of
chlorobenzenes.
K105
Separated aqueous stream from the reactor
(T)
product washing step in the production of
chlorobenzenes.
1107
Column
bottoms
from
product
separation
from
(C,T)
the production of 1,1-dimethylhydrazine
(UDNH)
from carboxylic acid hydrazides.
1108
Condensed
column
overheads
from product
(I,T)
separation
and
condensed
reactor vent gases
from
the
production
of
1,1-dimethylhydrazine
(UDNH)
from carboxylic acid hydrazides.
1109
Spent filter cartridges from the product
(T)
purification
from
the
production
of
1,1-di-
methyihydrazine
(UDMH)
from carboxylic acid
hydraz ides.
1110
Condensed column overheads from intermediate
(T)
separation from the production of 1,1-di—
iaethylhydrazine
(UDMH)
from carboxylic acid
hydraz ides.
Kill
Product
wastewaters
from
the
production
of
(C,T)
dinitrotoluene via nitration of toluene.
1112
Reaction by-product water from the drying
(T)
column in the production of toluenediamine
via hydrogenation of dinitrotoluene.
1113
Condensed liquid light ends from the
(T)
purification of toluenediamine in the
production of toluenediamine via
hydrogenation
of
dinitroluene.
128—585
116
K1l4
Vicinals from the purification of toluene-
(T)
diamine in the production of toluenediamine
via hydrogenation of dinitrotolune.
K115
Heavy
ends
from
the
purification
of
(T)
toluenediamine in the production of
toluenediamine via hydrogenation of di-
nitrotoluene.
K116
Organic condensate from the solvent recovery
(T)
column in the production of toluene di’—
isocyanate via phosgenation of toluenedi-
amine.
1117
Wastewater from the reactor vent gas
(T)
scrubber in the production of ethylene di-
bromide via bromination of ethene.
K118
Spent adsorbent solids from purification of
(T)
ethylene dibromide in the production of
ethylene dibromide via bromination of
ethene.
K136
Still bottoms from the purification of
(T)
ethylene
-dibromide
in
the
production
of
ethylene dibromide via bromination of
ethene.
Inorganic
Chemicals:
1071
Brine purification muds from the mercury
(T)
cell process in chlorine production, where
separately prepurified brine
is not used.
K073
Chlorinated hydrocarbon waste from the
(T)
purification step of the diaphragm cell
process
using graphite anodes in chlorine
production.
1106
Wastewater treatment sludge from the mercury
(T)
cell process in chlorine production.
Pesticides:
K031
By-product salts generated in the production
(T)
of MSMA and cacodylic acid.
1032
Wastewater treatment sludge from the
(T)
production of chlordane.
128—586
117
1033
Wastewater and scrub water from the
(T)
chlorination
of
cyclopentadiene
in
the
production of chlordane.
1034
Filter solids from the filtration of hexa-
(T)
chiorocyclopentadiene in the production of
chiordane.
1097
Vacuum stripper discharge from the chlordane
(T)
chlorinator in the production of chiordane.
1035
Wastewater
treatment
sludges
generated
in
(T)
the production of creosote.
1036
Still
bottoms
from
toluene
reclamation
(T)
di~ti1lation
in
the
production
of
di-
sulfoton.
K037
Wastewater treatment sludges from the
(T)
production
of
disulfoton.
1038
Wastewater
from
the
washing’
and
stripping
of
(T)
phorate
production.
1039
Filter cake from the filtration of diethyl—
(T)
phosphorodithioic acid in the production of
phorate.
1040
Wastewater
treatment
sludge
from
the
(T)
production of phorate.
1041
Wastewater treatment sludge from the
(T)
production
of
toxaphene.
1098
Untreated
process
wastewater
from
the
(T)
production
of
toxaphene.
1042
Heavy ends or distillation residues from the
(T)
distillation of tetrachlorobenzene in the
production
of
2,4,5-T.
1043
2,6-Dichlorophenol waste from the production
(T)
of 2,4—D.
1099
Untreated wastewater from the production of
(T)
2 ,4—D.
K123
Process wastewater (including supernates,
(T)
filtrates and washwaters)
from the
production of ethylenebisdithiocarbamic acid
and its salts.
128—587
118
1124
Reactor vent scrubber water from the
(C,T)
production of ethylenebisdithiocarbamic acid
and its salts.
1125
Filtration,
evaporation and centrifugation
(T)
solids from the production of ethylenebisdi—
thiocarbamic acid arid its salts.
1126
Bag~iousedust and floor sweepings in milling
(T)
and packaging operations from the production
or formulation of ethylenebisdithiocarbamic
acid and its salts.
1131
Wastewater from the reactor and spent
(C,T)
sulfuric acid from the acid dryer from the
production of methyl bromide.
1132
Spent absorbent and wastewater separator
(T)
solids from the production of methyl
bromide.
Explosives:
1044
Wastewater treatment sludges from the
(R)
manufacturing and processing of explosives.
1045
Spent carbon from the treatment of
(R)
wastewater containing explosives.
1046
Wastewater treatment sludges from the
(T)
manufacturing, formulation and loading of
lead-based initiating compounds.
1047
Pink/red water from TNT operations.
(R)
Petroleum Refining:
1048
Dissolved air flotation (DAF)
float from the
(T)
petroleum refining industry.
1049
Slop oil emulsion solids from the petroleum
(T)
refining industry.
1050
Heat exchanger bundle cleaning sludge from
(T)
the petroleum refining industry.
1051
API
separator sludge from the petroleum
(T)
refining industry.
K052
Tank bottoms
(leaded) from the petroleum
(T)
refining industry.
128—588
119
Iron and Steel:
1061
Emission control dust/sludge from the
(T)
primary production of steel in electric
furnaces.
K062
Spent pickle liquor generated by steel
(C,T)
finishing operations of facilities within
the iron and steel industry
(SIC Codes 331
and 332)
(as defined in 35 Ill. Ada. Code
720.110).
Primary
Copper:
1064
Acid plant blowdown slurry or sludge
(T)
resulting from the thickening of blowdown
slurry
from
primary
copper
production.
Primary
Lead:
1065
Surface impoundment solids contained in and
(T)
dredged from surface impoundments at primary
lead smelting facilities.
Primary Zinc:
K066
Sludge
from
treatment
of
process
wastewater
(T)
or
acid
plant
blowdown
from
primary
zinc
production.
BOARD NOTE:
This
waste
listing
is
the
subject
of
a
judicial
remand
in
American
Mining
Congress
v.
EPA,
907
F.2d
1179
(D.D.C.
1990).
The
Board
intends
that
this
listing
not
become
enforceable
in
Illinois
until
the
first
date
upon
which
the
Board
RCRA
program
becomes
“not
equivalent
to
the
Federal
program,”
within
the
meaning
of
Section
3006(b)
of
the
RCRA
Act,
42
U.S.C;
6926(b),
the
Board
RCRA
rules become
“less
stringent”
than
the
USEPA rules,
as this phrase is used in Section 3009,
42 U.S.C.
6929,
or
the
Board
RCRA
rules are not
“identical
in
substance”
with the federal rules as that term is intended by Ill. Rev.
Stat.
1989 ch.
111 1/2, pars.
1007.2 and 1022.4 as a result of
some action by USEPA with regard to this listing in responsá to
the American Mining Congress remand.
Primary Aluminum:
1088
Spent potliners from primary aluminum
(T)
reduction.
128—589
120
Ferroalloys:
1090
Emission control dust or sludge from
(T)
ferrochromiumsilicàn production.
1091
Emission control dust or sludge from
(T)
ferrochromium production.
Secondary Lead:
1069
Emission control dust/sludge from secondary
(T)
lead smelting.
BOARD
NOTE:
This listing is
administratively stayed for sludge generated
from
secondary
acid
scrubber
systems.
The
stay will remain in effect until this note
is removed.
K100
Waste leaching solution from acid leaching
(T)
of emission control dust/sludge from
secondary lead smelting.
Veterinary Pharmaceuticals:
1084
Wastewater
treatment
sludges
generated
(T)
during the production of veterinary
pharmaceuticals from arsenic or organo-
arsenic compounds.
1101
Distillation tar residues from the
(T)
distillation of aniline-based compounds in
the production of veterinary pharmaceuticals
from arsenic or organoarsenic compounds.
1102
Residue from use of activated carbon for
(T)
decolorization in the production of
veterinary pharmaceuticals from arsenic or
organo—arsenic compounds.
Ink
Formulation:
1086
Solvent washes and sludges, caustic washes
(T)
and sludges, or water washes and sludges
from
cleaning
tubs
and
equipment
used
in
the
formulation of
ink
from pigments, driers,
soaps and stabilizers containing chromium
and lead.
128—590
121
Coking:
1060
Ammonia still lime sludge from coking
(T)
operations.
K087
Decanter tank tar sludge from coking
(T)
operations.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
128—591
122
TITLE 35:
ENVIRONMENTAL
PROTECTION
SUBTITLE G:
WASTE
DISPOSAL
CHAPTER I:
POLLUTION
CONTROL
BOARD
SUBCHAPTER
c:
HAZARDOUS WASTE OPERATING REQUIREMENTS
PART
722
STANDARDS
APPLICABLE
TO
GENERATORS
OF
HAZARDOUS
WASTE
SUBPART
A:
GENERAL
Section
722.
iid
722.111
722.112
Section
722.120
722.121
722.122
722.123
Section
722.130
722. 131
722.132
722.133
722. 134
Section
722.140
722.141
722.142
722.143
722.144
Section
722.150
722.151
722.152
722.153
722. 154
722.155
722
.
156
722 .157
Purpose,
Scope and Applicability
Hazardous Waste Determination
USEPA Identification Numbers
SUBPART B:
THE MANIFEST
General Requirements
Acquisition of Manifests
Number
of
Copies
Use of the Manifest
SUBPART C:
PRE-TRANSPORT REQUIREMENTS
Packaging
Labeling
Marking
Placarding
Accumulation
Time
SUBPART
D:
RECORDKEEPING
AND
REPORTING
Recordkeeping
Annual Reporting
Exception Reporting
Additional Reporting
Special
Requirements
for Generators of between 100 and
1000 kilograms per month
SUBPART
E:
EXPORTS OF HAZARDOUS WASTE
Applicability
Definitions
General Requirements
Notification of Intent to Export
Special Manifest Requirements
Exception Report
Annual Reports
Recordkeeping
128—592
123
SUBPART
F:
IMPORTS
OF
HAZARDOUS
WASTE
Section
722.160
Imports of Hazardous Waste
SUBPART
G:
FARMERS
Section
722.170
Farmers
Appendix A
Hazardous Waste Manifest
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
111½, pars.
1022.4
and
1027).
SOURCE:
Adopted
in
R81—22,
43
PCB
427,
at
5
Ill.
Reg.
9781,
effective as noted in 35 Ill.
Ada. Code 700.106; amended and
codified in R8l—22, 45 PCB 317,
at- 6
Iii. Reg.
4828, effective as
noted
in 35 Ill. Ada. Code 700.106; amended in R82-18,
51 PCB 31,
at
7 Ill. Reg.
2518,
effective February 22,
1983; amended in R84-
9 at 9
Ill.
Reg.
11950, effective July 24,
1985; amended in R85-
22 at 10 Ill.
Reg.
1131, effective January 2,
1986; amended in
R86—l at 10 Ill.
Reg.
14112, effective August 12,
1986;
amended
in R86—l9 at 10 Ill.
Reg.
20709, effective December 2,
1986;
amended in R86—46 at 11 Ill. Reg.
13555,
effective August
4,
1987; amended in R87—5at 11 Ill.
Reg.
19392, effective November
12,
1.987;
amended in R87—39 at 12 Ill. Reg.
13129,
effective July
29,
1988;
amended in R88—16 at 13
Ill.
Reg.
452, effective
December 27,
1988; amended in R89—1 at 13 Ill.
Reg.
18523,
effective November 13, 1989; amended in R90-10 at 14 Ill. Reg.
16653,
effective
September
25,
1990;
amended
in
R90—11
at
15
Ill.
Reg.
9644, effective June 17,
1991; amended in R91-1 at 15 Ill.
Reg.
14562, effective October
1,
1991;
amended
in
R91—13
at
16
Ill.
Reg.
,
effective
SUBPART A:
GENERAL
Section 722.110
Purpose, Scope and Applicability
a)
These regulations establish standards for generators of
hazardous waste.
b)
A generator who treats, stores or disposes of hazardous
waste on-site must only comply with the following
Sections of this Part with respect to that waste:
Sectign 722.111 for determining whether or not the
generator has a hazardous waste,
Section 722.112 for
obtaining an EPA identification number, Section
722.140(c)
and
(d)
for
recordkeeping,
Section
722.143
for additional reporting and,
if applicable,
Section
722.170 for farmers.
C)
Any pefson
who
imports
hazardous
waste into the United
128—593
124
States must comply with the standards applicable to
generators established in this Part.
d)
A farmer who generates waste pesticides which are
hazardous waste and’who complies with all of the
requirements of Section 722.151 is not required to
comply with other standards in this Part,
or 35 Ill.
Ada. Code 702, 703,
724 725 or 728 with respect to such
pesticides.
e)
A person who generates a hazardous waste as defined by
35
Ill.
Ada.
Code 721 is subject to the compliance
requirements and penalties prescribed in Title VIII and
XII of the Environmental Protection Act if he does not
comply with the requirements of this Part.
(Board Note:
A gcncrator who treats,
stores or
disposes of hazardous waste on—site
the applicable standards and permit
must comply
requirements
with
set
,
.—.,
f)
An
owner
or
operator
who
initiates
a
shipment
of
hazardous waste from a treatment, storage or disposal
facility must comply with the generator standards
established in this Part.
-(-Beard
NOteBOARD
NOTE:
The provisions of Section
722.134 are applicable to the on-site accumulation of
hazardous waste by generators.
Therefore, the
provisions of Section 722.134 only apply to owners or
operators who are shipping hazardous waste which they
generated at that facility.
A generator who treats.
stores or disposes of hazardous waste on—site must
comply with the applicable standards and permit
recniirements set forth in 35 Ill. Ada. Code 702, 703,
724,
725, 726 and 728.)-
g)
35 Ill.
Ada.
Code 700 contains rules on application of
other Board regulations.
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
Section 722.134
Accumulation Time
a)
Except as provided in subsections
(d),
(e) or
(f), a
generator is exempt from all the requirements in 35
Ill.
Ada. Code 725.Subparts G and H, except for 35
Ill.
Ada.
Code 725.211 and 725
•
214 and may accumulate
hazardous waste on—site for 90 days or less without a
permit
or
without
having
interim status, provided that:
128—594
125
1)
The waste is placed:
A)
In containers and the generator complies with
35
Ill. Ada. Code 725.Subpart I;
or
B)
In
tanks
and the generator complies with 35
Ill. Ada. Code 725.Subpart J except 35 Ill.
Ada.
Code 725.297(c) and 725.300;
or
C)
On drip pads and the generator complies with
35
Ill.
Ada.
Code
725.Subpart
W
and
maintains
the following records at the facility:
i)
A description of the procedures that
will, be followed to ensure that all
wastes are removed from the drip pad and
associated collection system at least
once every 90 days;
arid
ii)
Documentation of each waste removal,
including the quantity of waste removed
from the drip pad and the sump or
collection system .and the date and time
of
removal.
BOARD NOTE:
The
“in
addition”
hanging
paragraph is in the introduction to
subsection
(a).
2)
The date upon which each period of accumulation
begins is clearly marked and visible for
inspection
on
each
container;
3)
While being accumulated on—site, each container
and tank is labeled or marked clearly with the
words,
“Hazardous
Waste”,
and
4)
The generator complies with the requirements for
owners or eperators in 35 Ill. Ada. Code
725.Subparts C and D, with 35 Ill.
Ada. Code
725.116 and 728.107(a) (4).
b)
A generator who accumulates hazardous waste’for more
than 90 days is an operator of a storage facility and
is subject to the requirements of 35 Ill. Ada. Code 724
and 725 and the permit requirements of 35 Ill. Ada.
Code 702,
703 and 705 unless the generator has been
granted
an
extension
of
the
90-day period.
If
hazardous wastes must remain on—site for longer than 90
days due to unforeseen, temporary, and uncontrollable
circumstances,
the
generator
may
seek
an
extension
of
up to 30 days by means of a variance or provisional
128—595
12 6
variance, pursuant to Section 37 of the Environmental
Protection Act.
c)
Accumulation near point of generation.
1)
A
generator
may
accumulate
as
much
as
55
gallons
of
hazardous
waste
or
one
quart
of
acutely
hazardous waste listed’ in 35 Ill. Adm. Code
721.133(e)
in containers’ at or near any point of
generation where wastes initially accumulate,
which is under the control of the operator of the
process generating the waste, without a permit or
interim
status
and
without
complying
with
paragraph
(a) provided the generator:
A)
Complies
with
35
Ill.
Ada.
Code
725.271,
725.272 and 725.273(a); and
B)
marks the generator’s containers either with
the words “Hazardous Waste” or with other
words that identify the contents of the
containers.
2)
A generator who accumulates either hazardous waste
or
acutely
hazardous
waste
listed
in
35 Ill. Ada.
Code 721.133(e)
in excess of the amounts listed in
subsection
(c) (1) at or near any point of
generation must, with respect to that amount of
excess waste, comply within three days with
subsection
(a) or other applicable provisions of
this chapter.
During the three day period the
generator must continue to comply with subsection
(c) (1).
The generator must mark the container
holding the excess accumulation of hazardous waste
with the date the excess amount began
accumulating.
d)
A generator who generates greater than 100 kilograms
but less than 1000 kilograms of hazardous waste in a
calendar month may accumulate hazardous waste on—site
for 180 days or less without a permit or without having
interim status provided that:
1)
The quantity of waste accumulated on—site never
exceeds 6000 kilograms;
2)
The generator complies with the requirements of 35
Ill. Ada. Code 725.Subpart I, except the generator
need not comply with 35 Ill. Ada. Code 725.276;
3)
The generator complies with the requirements of 35
Ill.
Ada.
Code
725.301;
128—596
127
4)
The
generator
complies
with
the
requirements
of
subsections
(a) (2) and -(a-)-(3),~and the
requirements of 35 Ill.
Ada.
Code 725.Subpart C
and of 35 Ill.
Ada. Code 728.107(a) (4) and
5)
The generator complies with the following
requirements:
A)
At all times there must be at least one
employee either on the premises or on call
(i.e., available to respond to an emergency
by reaching the facility within a short
period of time) with the responsibility for
coordinating all emergency response measures
specified
in
subsection
(d) (4) (D).
The
employee is the emergency coordinator.
B)
The
generator
shall post the following
information next to the telephone:
i)
The name and telephone number of the
emergency coordinator:
ii)
Location
of
fire
extinguishers
and
spill
control
material,
and
if
present,
fire
alarm:
and
iii) The telephone number of the fire
department, unless the facility has a
direct alarm.
C)
The generator shall ensure that all employees
are thoroughly familiar with proper waste
handling and emergency procedures, relevant
to their responsibilities during normal
facility operations and emergencies:
D)
The emergency coordinator or designee shall
respond to any emergencies that arise.
The
applicable responses are as follows:
i)
In the event of a fire,
call the fire
department or attempt to extinguish’ it
using
a
fire
extinguisher:,
ii)
In the event of a spill, contain the
flow of hazardous waste to the extent
possible, and as soon as is practicable,
clean up the hazardous waste and any
contaminated materials or soil:
128—59 7
128
iii) In the event of a fire, explosion or
other release which could threaten human
health outside the facility or when the
generator has knowledge that a spill has
reached surface water, the generator
shall immediately notify the National
Response Center
(using its 24-hour toll
free number 800/424—8802).
The report
must include the following information:
the name, address and USEPA
identification
number
(35 ill. Ada. Code
722.112) of the generator;
date, time
and
type
of incident
(e.g.,
spill or
fire); quantity and
type
of
hazardous
waste involved in the incident; extent
of injuries,
if any; and, estimated
quantity and disposition of recoverable
materials,
if any.
e)
A
generator
who
generates
greater
than
100 ‘kilograms
but less than 1000 kilograms of hazardous waste in a
calendar month and who must transport the waste, or
offer the waste for transportation,,
over a distance of
200 miles or more for off—site treatment,
storage or
disposal may-accumulate hazardOus waste on—site for 270
days or less without a permit or without having interim
status provided that the generator complies with the
requirements of subsection
(d).
f)
A generator who generates greater than 100 kilograms
but less than 1000 kilograms of hazardous waste in a
calendar month and who accumulates hazardous waste in
quantities exceeding 6000 kg or accumulates hazardous
waste for more than 180 days
(or for more than 270 days
if the generator must transport the waste,
or offer the
waste for transportation, over a distance of 200 miles
or more)
is an operator of a storage facility and is
subject to the requirements of 35 Ill. Ada. Code 724
and 725 and the permit requirements of 35 Ill. Adm.
Code 703 unless the generator has been granted an
extension to the 180-day
(or 270-day if applicable)
period.
If hazardous wastes must remain on—site for
longer than 180 days
(or 270 days if applicable)
due to
unforeseen,
temporary and uncontrollable circumstances,
the generator may seek an extension of up. to 30 days by
means of variance or provisional variance pursuant to
Section 37 of the Environmental Protection Act.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
128—598
129
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE
G:
WASTE
DISPOSAL
CHAPTER
1:
POLLUTION CONTROL BOARD
SUBCHAPTER
C:
HAZARDOUS
WASTE
OPERATING
REQUIREMENTS
PART 724
STANDARDS
FOR
OWNERS
AND
OPERATORS
‘OF
HAZARDOUS
WASTE
TREATMENT,
STORAGE AND DISPOSAL FACILITIES
SUBPART A:
GENERAL PROVISIONS
Purpose, Scope and Applicability
Relationship to Interim Status Standards
SUBPART
B:
GENERAL
FACILITY
STANDARDS
Applicability
Identification Number
Required
Notices
General Waste Analysis
Security
General
Inspection
Requirements
Personnel
Training
General
Requirements
for
Ignitable,
Reactive
or
Incompatible
Wastes
724.118
Location
Standards
Section
724.130
724.131
724. 132
724
.
133
724.134
724.135
724.137
SUBPART C:
PREPAREDNESS AND PREVENTION
Applicability
Design
and
Operation
of
Facility
Required
Equipment
Testing and Maintenance of Equipment
Access
to
Communications
or
Alarm
System
Required
Aisle
Space
Arrangements
with
Local
Authorities
SUBPART
D: CONTINGENCY
PLAN
AND EMERGENCY PROCEDURES
Section
724
.
150
724
.
151
724.152
724. 153
724.154
724.155
724.
156
Applicability
Purpose and Implementation of Contingency Plan
Content
of Contingency Plan
Copies of Contingency Plan
Amendment of Contingency Plan
Emergency Coordinator
Emergency Procedures
Applicability
Use of Manifest System
Manife~tDiscrepancies
Section
724. 101
724.103
Section
724.110
724.
111
724.112
724.
113
724.114
724. 115
724.116
724. 117
Section
724. 170
724.171
724. 172
SUBPART
E:
MANIFEST SYSTEM,
RECORDKEEPING
AND
REPORTING
128—599
130
Operating
Record
Availability,Retention and Disposition of Records
Annual Report
Urnnanifested Waste Report
Additional Reports
SUBPART
F:
RELEASES FROM SOLID WASTE MANAGEMENT UNITS
Section
724.
190
724.
191
7~4.192
724.
193
724.
194
724.195
724.196
724.197
724.198
724.199
724.200
724.201
Section
724.240
724.241
724.242
724. 243
724.244
724 .245
724. 246
Applicability
Required Programs
Groundwater Protection Standard
Hazardous Constituents
Concentration Limits
Point of Compliance
Compliance Period
General
Groundwater
Monitoring
Requirements
Detection Monitoring Program
Compliance Monitoring Program
Corrective Action Program
Corrective Action for Solid Waste Management Units
SUBPART G:
CLOSURE AND POST-CLOSURE
Applicability
Closure Performance Standard
Closure
Plan;
Amendaent
of
Plan
Closure;
Time
Allowed
For
Closure
Disposal
or
Decontamination
of
Equipment,
Structures
and Soils
Certification
of
Closure
Survey Plat
Post-closure Care and Use of Property
Post—closure Plan; Amendment of Plan
Post—closure Notices
Certification of Completion of Post—closure Care
SUBPART
H:
FINANCIAL REQUIREMENTS
Applicability
Definitions of Terms As Used In This Subpart
Cost Estimate for Closure
Financial Assurance for Closure
Cost Estimate for Post—closure Care
Financial Assurance for Post—closure Care
Use of a Mechanism for Financial Assurance of Both
Closure and Post—closure Care
Liability Requirements
Incapacity of Owners or Operators, Guarantors or
Financial Institutions
724.251
Wording of the Instruments
724.173
724.174
724.175
724.176
724.177
Section
724.210
724.211
724.212
724.213
724 .214
724.215
724.216
724.217
724.218
724 .219
724.220
724.247
724.248
128—600
131
SUBPART
I:
USE
AND
MANAGEMENT
OF
CONTAINERS
Section
724 .270
724.271
724.272
724.273
724.274
724.275
724.276
724.277
724.278
Section
724.290
724.291
724.292
724.293
724.294
724.295
724.296
724. 297
724. 298
724.299
724.300
Applicability
Condition of Containers
Compatibility of Waste With Container
Management of Containers
Inspections
Containment
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Closure
SUBPART 3:
TANK SYSTEMS
Applicability
Assessment of Existing Tank System’s Integrity
Design
and
Installation
of New Tank Systems or
Components
Containment and Detection of Releases
General Operating Requirements
Inspections
Response to Leaks or Spills and Disposition of Leaking
or unfit—for—use Tank Systems
Closure and Post—Closure Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Special
Requirements
for Hazardous Wastes F020,
F021,
F022,
F023,
F026
and
F027
SUBPART
K:
SURFACE
IMPOUNDMENTS
Applicability
Design and Operating Requirements
Double-lined Surface Impoundments:
Exemption from
Subpart
F:
Ground-water
Protection
Requirements
(Repealed)
Monitoring
and
Inspection
Emergency
Repairs;
Contingency
Plans
Closure
and
Post-closure
Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Special Requirements for Hazardous Wastes F020,
F021,
F022, F023,
F026 and F027
SUBPART L:
WASTE PILES
Section
724.350
Applicability
724.351
Design
arid
Operating
Requirements
724.352
Double-lined Piles:
Exemption from Subpart
F:
water Protection Requirements
(Repealed)
724.353
Inspection
of Liners:
Exemption from Subpart F:
Ground—water Protection Requirements
(Repealed)
Section
724.320
724. 321
724.322
724.326
724.327
724.328
724
•
329
724.330
724.331
Ground—
128—601
132
Monitoring and Inspection
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Closure and Post—closure Care
Special Requirements for Hazardous Wastes F020,
F021,
F022, F023, F026 and F027
Section
724.370
724.371
724.372
724.373
724.376
724.378
724.
379
724.380
724.381
724.382
724.383
SUBPART
M:
LAND
TREATMENT
Applicability
Treatment Program
Treatment Demonstration
Design and Operating Requirements
Food—chain Crops
Unsaturated Zone Monitoring
Recordkeeping
Closure and Post—closure Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Special Requirements for Hazardous Wastes F020,
F021,
F022,
F023, F026 and F027
SUBPART N:
LANDFILLS
Section
724.400
Applicability
724.401
Design and Operating Requirements
724.402
Double-lined Landfills:
Exemption from Subpart F:
Ground-water Protection Requirements
(Repealed)
Monitoring and Inspection
Surveying and Recordkeeping
Closure and Post—closure Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Special Requirements for Bulk and Containerized Liquids
Special Requirements for Containers
Disposal of Small Containers of Hazardous Waste in
Overpacked Drums
(Lab Packs)
724.417
Special Requirements for Hazardous Wastes F020,
F02l,
F022,
F023,
F02-6 and F027
SUBPART 0:
INCINERATORS
724.440
724.441
724.442
724.443
724.444
724.445
724. 447
724.451
Applicability
Waste Analysis
Principal Organic Hazardous Constituents (POHCs)
Performance Standards
Hazardous Waste Incinerator Permits
Operating Requirements
Monitoring and Inspections
Closure
724
•
354
724.356
724.357
724.358
724.359
724.403
724.409
724.410
724.412
724.413
724.4 14
724.415
724. 416
Section
128—602
133
Applicability
Assessment of existing drip pad integrity
Design and installation of new drip pads
Design and operating requirements
Inspections
Closure
SUBPART
X:
MISCELLANEOUS
UNITS
Section
724.701
Applicability
724.701
Environmental Performance Standards
724.702
Monitoring,
Analysis, Inspection, Response, Reporting
and Corrective Action
724.703
Post-closure
Care
SUBPART AA:
AIR EMISSION
STANDARDS
FOR
PROCESS
VENTS
Applicability
Definitions
Standards:
Process Vents
Standards:
Closed-vent Systems and Control Devices
Test methods and procedures
Recordkeeping requirements
Reporting
R~equirements
SUBPART BB:
AIR EMISSION STANDARDS
FOR EQUIPMENT
LEAXS
Applicability
Definitions
Standards:
Standards:
Standards:
Service
Standards:
Sampling Connecting Systems
Standards:
Open—ended Valves or Lines
Standards:
Valves in Gas/Vapor or Light Liquid Service
Standards:
Pumps, Valves, Pressure’ Relief Devices and
Other Connectors
Standards:
Delay of Repair
Standards:
Closed—vent Systems and Control Devices
Alternative Percentage Standard for Valves
Skip Period Alternative for Valves
Test
Methods
and
Procedures
Recordkeeping
Requirements
Reporting Requirements
Appendix A
Recordkeeping Instructions
Appendix B
EPA Report Form and Instructions
(Repealed)
Appendix D
Cochran’s Approximation to the Behrens-Fisher
Student’s T-Test
SUBPART
W:
Section
724.670
724.671
724.
672
724.
673
724
.
674
724
.
675
DRIP PADS
Section
724 .930
724.931
724 .932
724.933
724.934
724.935
724.936
Section
724.950
724. 951
724.952
724.953
724.954
724.955
724.956
724.957
724.958
724.959
724.960
724.961
724.962
724.963
724.964
724.965
Pumps
in
Light
Liquid
Service
Compressors
Pressure Relief Devices in Gas/Vapor
128—603
134
Appendix E
Examples of Potentially Incompatible Waste
Appendix I
Groundwater Monitoring List
AUTHORITY:
Implementing
Section
22.4
and
authorized
by
Section
27 of the Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
111½,
pars.
1022.4 and 1027).
SOURCE:
Adopted in R82—19,
53 PCB 131,
at
7
Ill. Reg.
14059,
effective October 12,
1983; amended in R84—9 at 9
Ill.
Reg.
11964, effective July 24,
1985; amended in R85-22 at 10 Ill. Reg.
1136, effective January
2,
1986; amended in R86-1 at 10
Ill. Reg.
14119, effective August 12,
1986; amended in R86—28 at 11 Ill.
Reg.
6138, effective March 24,
1987;
amended in R86-28 at 11 Ill.
Reg. 8684, effective April
21,
1987;
amended in R86—46 at 11 Ill.
Reg. 13577,
effective August
4,
1987; amended in R87—5 at 11 Ill.
Reg.
19397,
effective November 12,
1987; amended in R87-39 at 12
Ill. Reg.
13135, effective July 29,
1988;
amended
in
R88-16
at
13
Ill.
Reg.
458,
effective
December
28,
1988;
amended
in
R89-1
at
13
Ill. Reg.
18527, effective November 13,
1989; amended in R90-2
at 14 Ill. Reg.
14511, effective August 22,
1990;
amended in R90-
10
at
14
Ill.
Reg.
16658,
effective
September
25,
1990;
amended
in R90—11 at 15
Ill. Reg.
9654, effective June 17,
1991; amended
in R91—l at 15 Ill.
Reg.
14572, effective October
1,
1991;
amended in R91-13 at 16 Ill. Reg.
,
effective
SUBPART
G:
CLOSURE
AND
POST-CLOSURE
Section 724.212
Closure Plan; Amendment of Plan
a)
Written Plan.
1)
The owner or operator of a hazardous waste
management facility shall have a written closure
plan.
In addition, certain surface impoundments
and waste piles from which the owner or operator
intends to remove or decontaminate the hazardous
waste at partial or final closure are required by
Sections 7.24.328(c)(1)(A)
and 724.358(c)(1)(A)
to
have contingent closure plans.
The plan must be
submitted with the permit application,
in
accordance with 35 Ill. Ada. Code 703.183, and
approved by the Agency as part of the permit
issuance proceeding under 35 Ill. Ada. Code 705.
In accordance with 35 Ill. Ada. Code 703.241, the
approved closure plan will become a condition of
any RCRA permit.
2)
The Agency’s approval of the plan must ensure that
the approved àlosure plan is consistent with
Sections 724.211 through 724.215 and the
applicable requirements of Sections 724.190 et
128—604
135
seq.,
724.278,
724.297,
724.328, 724.358,
724.380,
724.410,
724.451
and
724.701.
Until
final
closure
is
completed
and
certified
in
accordance
with
Section
724.515,
a
copy
of
the approved plan and
approved revisions must be furnished to the Agency
upon request,
including requests by mail.
b)
Content
of
plan.
The
plan
must identify steps
necessary to perform partial or final closure of the
facility at any point during its active life.
The
closure
plan
must
include,
at
least:
1)
A
description
of
how
each
hazardous
waste
management unit at the facility will be closed in
accordance
with
Section
724.211;
2)
A description of how final closure of the facility
will be conducted in accordance with Section
724.211.
The
description
must
identify
the
maximum
extent
of
the
operations
which
will
be
unclosed
during
the
active
life
of
the
facility;
and
3)
An estimate of the maximum inventory of hazardous
wastes
ever
on—site
over
the
active
life
of
the
facility and a detailed description of the methods
to
be
used
during
partial
closures
and
final
closure,
including,
but
not
limited
to,
methods
for
removing,
transporting, treating, storing or
disposing of all hazardous wastes, and
identification of the type(s)
of off-site
hazardous waste management units to be used,
if
applicable;
and
4)
A detailed description of the steps needed to
remove or decontaminate all hazardous waste
residues
and
contaminated
containment
system
components,
equipment, structures and soils during
partial
and
final closure, including, but not
limited to, procedures for cleaning equipment and
removing contaminated soils, methods for sampling
and testing surrounding soils and criteria for
determining
the
extent
of
decontamination
required
to satisfy the closure performance standard; and
5)
A detailed description
of, other activities
necessary during the closure period to ensure that
all partial closures, and final closure satisfy the
closure performance standards,
including, but not
limited to, groundwater monitoring,
leachate
collection, and run—on and run—off control; and
128—605
136
6)
A schedule for closure of each hazardous waste
management unit and for final closure of the
facility.
The schedule must include,
at
a
minimum,
the
total
time
required
to
close
each
hazardous waste management unit and the time
required for intervening closure activities which
will allow tracking of the progress of partial and
final closure.
(For example,
in the case of a
landfill unit, estimates of the time required to
treat and dispose of all hazardous waste inventory
and of the time required to place a final cover
must be included.)
7)
For
facilities
that
use
trust
funds
to
establish
financial assurance under Section 724.243 or
724.245 and that are expected to close prior to
the expiration of the permit,
an estimate of the
expected year of final closure.
c)
Amendment of the plan.
The owner or operator shall
submit a written notification of or request for a
permit modification to authorize a change in operating
plans, facility design or the approved closure plan in
accordance with the applicable procedures in 35
Ill.
Ada. Code 702,’ 703 and 705.
The written notification
or request must include a copy of the amended closure
plan for review or approval by the Agency.
1)
The owner or operator may submit a written
notification or request to the Agency for a permit
modification to amend the closure plan at any time
prior to notification of partial or final closure
of the facility.
2)
The owner or operator shall submit a written
notification of or request for a permit
modification to authorize a change in the approved
closure plan whenever:
A)
Changes in operating plans or facility design
affect the closure plan;
or
B)
There is a change in the expected year of
closure,
if applicable,
or
C)
In conducting partial or final closure
activities, unexpected events require
modification of the approved closure plan.
3)
The owner or operator shall submit a written
request for a permit modification including a copy
of the amended closure plan for approval at least
128—606
137
60 days prior to the proposed change in the
facility design or operation, or no later thar
days after an unexpected event has occurred wi
has affected the closure plan.
If an unexpect
event occurs during the partial or final c1oS1~
period, the owner or operator shall request a
permit modification no later than 30 days
aftE
the unexpected event.
An
owner
or operator of
surface impoundment or waste pile that intendE
remove
all hazardous waste at closure and is r
otherwise
required
to
prepare
a
contingent
dc
plan under Sections 724.328(c) (1) (A),or
724.358(c) (1) (A), shall submit
an, amended c1o~
plan to the Agency no later than 60 days after
date the owner or operator or Agency determinE
that the hazardous waste management unit must
closed as a landfill, subject to the
requireine
of Section 724.410, or no later than 30 days
a
that date if the determination is made during
partial or final closure.
The Agency sball’
approve, disapprove or modify this amended pla
accordance with the procedures in 35 Ill. Ada.
Code 702, 703 and 705.
I-n accordance with 35
Adm.~Code702.160 and 703.241, the approved
closure plan will become a condition of any RC
permit issued.
4)
The Agency may request modifications to the p1
under the conditions described in Section
724.212(c) (2).
The owner or operator shall st
the modified plan within 60 days after the
Agency’s request,
or within 30 days if the cha
in facility conditions occurs during partial
c
final closure.
Any modifications requested b~
Agency must be approved in accordance
with
the
procedures
in
35
Ill.
Ada.
Code
702,
‘703
and
7
d)
Notification of partial closure and final closure.
1)
The
owner
or
operator
shall
notify
the
Agency
writing at least 60 days prior to
the
date on
which the owner or operator expects to begin
closure
of
a surface impoundment, waste pile,
treatment or landfill unit, or final closure c
facility with such a unit.
The owner or opera
shall notify the Agency in writing at’least 45
days prior to the date on which the owner or
operator expects to begin final closure of a
facility with only treatment or storage tanks,
container storage or incinerator units to be
closed.
The owner or operator shall notify th
Agency in writing at least 45 days prior to tI~
128—607
138
date on which the owner or operator exPects to
begin partial or final closure of a boiler or
industrial furnace
whichever is earlier.
2)
The date when the owner or operator “expects to
begin closure” must be either:
a)
No later than 30 days after the date on which
any hazardous waste management unit receives
the known final volume of hazardous wastes
or,
if there is a reasonable possibility that
the hazardous waste management unit will
receive additional hazardous wastes, no later
than one year after the date on which the
unit received the most recent volume of
hazardous waste.
If the owner or operator of
a hazardous waste management unit
demonstrates to the Agency that the hazardous
waste management unit or facility has the
capacity to receive additional hazardous
wastes and that the owner or operator have
taken, and will continue to take,
all steps
to prevent threats to human health and the
environment, including compliance with all
applicable permit requirements, the Agency
shall approve an extension to this one—year
limit.
Or,
B)
For units meeting the requirements of Section
724.213(d),
no later than 30 days after the
date on which the hazardous waste management
unit receives the final known volume of
non—hazardous wastes,
or,
if there is a
reasonable possibility that the hazardous
waste management unit will receive additional
non—hazardous wastes, no later than one year
after the date on which the unit received the
most recent volume of non—hazardous wastes.
If
the
onwer or operator demonstrates to the
Agency that the hazardous waste management
unit has the capacity to receive additional
non—hazardous wastes and that the owner and
operator have taken,
and will continue to
take, all steps to prevent threats to human
health and the environment, including
compliance with all applicable permit
requirements, the Agency shall approve an
extension to this one—year limit.
3)
If the facility’s permit is terminated, or if the
facility is’ otherwise ordered, by judicial decree
or Board order to cease receiving hazardous wastes
128—608
139
or to close,
then the requirements of this
subsection do not apply.
However, the owner or
operator shall close the facility in accordance
with the deadlines established in Section 724.213.
e)
Removal of wastes and decontamination or dismantling of
equipment.
Nothing
in this Section shall preclude the
owner or operator from removing hazardous wastes and
decontaminating or dismantling equipment in accordance
with the approved partial or final closure plan at any
time before or after notification of partial or final
closure.
(Source:
Amended at 16
Ill. Reg.
,
effective
)
SUBPART
0:
INCINERATORS
Section 724.440
Applicability
a)
The regulations in this Subpart apply to owners and
operators of facilities that incinerate hazardous waste
incinerators
(as defined in 35 Ill. Ada. Code 720.110),
except as Section 724.101 provides otherwise.
~e
following facility owners and operators arc considered
to incinerate hazardous waste:
1)
Owners or operators of hazardous waste
incinerators
(as defined
in
35 Ill.
Adin.
Code
720.110);
and
2)
Owners
or operators who burn hazardous waste in
boilers or in industrial furnaces
in order to
destroy them,
or who burn hazardous waste in
boilers or
in industrial furnaces for any
recycling purpose and elect to be regulated under
this Cubpart.
b)
After consideration of the waste analysis included with
Part B of the permit application, the Agency, in
establishing the permit conditions, must exempt the
applicant from all requirements of this Subpart except
Section 724.441
(Waste analysis) and Section 724.451
(Closure):
1)
If the Agency finds that the waste to be burned
is:
A)
Listed as a hazardous waste in 35 Ill. Adm.
Code 721, Subpart D solely because it is
ignitable
(Hazard Code I), corrosive (Hazard
Code C), or both;
or
128—609
140
B)
Listed as a hazardous waste in 35 Ill. Adm.
Code 721, Subpart D solely because it is
reactive (Hazard Code R) for characteristics
other than those listed in Section
721.123(a) (4) and (5), and will not be burned
when other hazardous wastes are present in
the combustion zone; or
C)
A hazardous waste solely because it possesses
the characteristic of ignitability,
corrosivity, or both,
as determined by the
test for characteristics of hazardous wastes
under 35 Ill. Ada. Code 721,
Subpart C; or
D)
A hazardous waste solely because it possesses
any of the reactivity characteristics
described by 35 Ill.
Adm. Code
721.123(a)(1),
(2),
(3),
(6),
(7)
and
(8)
and
will not be burned when other hazardous
wastes are present in the combustion zone;
and
2)
If the waste analysis shows that the waste
contains ‘none of the hazardous constituents listed
in 35 Ill. Adm. Code 721, Appendix H, which would
reasonably be expected to be in the waste.
c)
If the waste to be burned is one which is described by
subsections
(b) (1) (A),
(b) (1) (B),
(b) (1) (C)
or
(b) (1) (D) and contains insignificant concentrations of
the hazardous constituents listed in 35 Ill. Adm. Code
721, Appendix H, then the Agency may,
in establishing
permit conditions,
exempt the applicant from all
requirements of this Subpart, except Section 724.441
(Waste analysis) and Section 724.451
(Closure),
after
consideration of the waste analysis included with Part
B of the permit application, unless the Agency finds
that the waste .will pose a threat to human health or
the environment when burned in an incinerator.
d)
The owner or operator of an incinerator may conduct
trial burns subject only to the requirements of 35
Ill.
Ada. Code 703.222 through 703.225
(Short term and
incinerator permits).
(Source:
Amended at 16 Ill. Reg.
,
effective
)
SUBPART AA:
AIR EMISSION STANDARDS FOR PROCESS VENTS
Section
724.930
Applicability
128—610
141
a)
This Subpart applies to owners and operators of
facilities that treat,
store or dispose of hazardous
wastes
(except as provided in Section 724.101).
b)
Except for Sections 724.934(d) and 724.935(e), this
Subpart applies to process vents associated with
distillation, fractionation, thin—film evaporation,
solvent extraction, or air or steam stripping
operations that manage hazardous wastes with organic
concentrations of at least 10 ppmw (parts per million
by weight),
if these operations are conducted in:
1)
Units that are subject to the permitting
requirements of 35 Ill.
Ada. Code 703; or
2)
Hazardous waste recycling units that are located
on hazardous waste management facilities otherwise
subject
to
the
permitting
requirements
of
35
Ill.
Adm. Code 703.
c)
If
the
owner
or operator of process vents subject to
the requirements of Sections 724.932 through 724.936
has received a RCRA permit prior to December 21,
1990,
the requirements of Sections 724.932 through 724.936
must be incorporated when the ‘permit is reissued under
35 Ill.
Adin. Code 705.201 or reviewed under 35 Ill.
Ada. Code 702.161.
BOARD NOTE:
The requirements of Sections 724.932
through
724.936 apply to process vents on hazardous
waste recycling units previously exempt under 35 Ill.
Ada. Code 721.106(c)(l).
Other exemptions under 35
Ill. Ada. Code 721.104, 722.134 and
724.101(g)
are not
affected by these requirements.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
Section 724.935
Recordkeeping requirements
a)
Compliance Required.
1)
Each owner or operator subject to the provisions
of this Subpart shall comply with the
recordkeeping requirements of this Section.
2)
An owner or operator of more than one hazardous
waste
management unit subject to the provisions of
this
Subpart
may comply with the recordkeeping
requirements
for these hazardous waste management
uf~its in one recordkeeping system if the system
128—611
142
identifies each record by each hazardous waste
management unit.
b)
Owners and operators shall record the following
information in the facility operating record:
1)
For facilities that comply with the provisions of
Section 724.933 (a) (2), an implementation schedule
that includes dates by which the closed-vent
system and control device will be installed and in
operation.
The schedule must also include a
rationale of why the installation cannot be
completed at an earlier date.
The implementation
schedule must be in the facility operating record
by the effective date that the facility becomes
subject to the provisions of this Subpart.
2)
Up-to-date documentation of compliance with the
process vent standards in Section 724.932,
including:
A)
Information and data identifying all affected
process vents, annual throughput and
operating hours of each affected unit,
estimated emission rates for each affected
vent and for the overall facility (i.e.,
the
total emissions for all affected vents at the
facility), and the approximate location
within the facility of each affected unit
(e.g., identify the hazardous waste
management units on a facility plot plan).
B)
Information and data supporting determination
of vent emissions and emission reductions
achieved by add—on control devices based on
engineering calculations or source tests.
For the purpose of determining compliance,
determinations of vent emissions and emission
reductions must be made using operating
parameter values
(e.g., temperatures,
flow
rates, or vent stream organic compounds and
concentrations) that represent the conditions
that result in maximum organic emissions,
such as when the waste management unit
is.
operating at the highest load or capacity
level reasonably expected to occur.
If the
owner
or operator takes any action
(e.g.,
managing a waste of different composition or
increasing operating hours of affected waste
management units) that would result in an
increase in total organic emissions from
affected process vents at the facility, then
128—612
143
a new determination is required.
3)
Where
an
owner
or operator chooses to use test
data to determine the organic removal efficiency
or total organic compound concentration achieved
by the control device,
a performance test plan.
The test plan must include:
A)
A description of how it is determined that
the planned test is going to be conducted
when the hazardous waste management unit is
operating at the highest load or capacity
level reasonably expected to occur.
This
must include the estimated or design flow
rate and organic content of each vent stream
and define the acceptable operating ranges of
key process and control device parameters
during the test program.
B)
A detailed engineering description of the
closed—vent system and control device
including:
1)
Manufacturer’s name and model number of
control device.
ii)
Type of control device.
iii) Dimensions of the control device.
iv)
Capacity.
v)
Construction materials.
C)
A detailed description of sampling and
monitoring procedures,
including sampling and
monitoring locations in the system, the
equipment to be used,~samplingand monitoring
frequency,
and planned analytical procedures
for sample analysis.
4)
Documentation of compliance with Section 724.933
must include the following information’:
A)
A list of all information references and
sources used in preparing the documentation.
B)
Records~including the dates of each
compliance test required by Section
724.933(k).
C)
If engineering calculations are used,
a
128—6 13
144
design analysis, specifications,
drawings,
schematics,
and piping and instrumentation
diagrams based on the appropriate sections of
APTI Course 415 (incorporated by reference in
35 Ill. Ada. Code 720.111) or other
engineering texts,
approved by the Agency,
that present basic control device design
information.
Documentation provided by the
control device manufacturer or vendor that
describes the control device design in
accordance with subsections
(b) (4) (C) (i)
through
(vii) may be used to comply with this
requirement.
The design analysis must
address the vent stream characteristics and
control device operation parameters as
specified below.
i)
For a thermal vapor incinerator, the
design analysis must consider the vent
stream composition, constituent
concentrations and flow rate.
The
design analysis must also establish the
design minimum and average temperature
in the combustion zone and the
combustion zone residence time.
ii)
For a catalytic vapor incinerator, the
design analysis must consider the vent
stream composition, constituent
concentrations, and flow rate.
The
design analysis must also establish the
design minimum and average temperatures
across the catalyst bed inlet and
outlet.
iii)
For a boiler or process heater, the
design analysis must consider the vent
stream composition, constituent
•concentrations and flow rate.
The
design analysis must also establish the
design minimum and average flame ~zone
temperatures, combustion zone residence
time and description of method and
location where the vent stream is
introduced into the combustion zone.
iv)
For
a flare, the design analysis must
consider the vent stream composition,
constituent concentrations, and flow
rate.
The design analysis must also
consider the requirements specified in
Section 724.933(d).
128—6 14
145
v)
For a condenser, the design analysis
must consider the vent stream
composition, constituent concentrations,
flow rate,
relative humidity and
temperature.
The design analysis must
also establish the design outlet organic
compound concentration level,
design
average temperature of the condenser
exhaust vent stream and design average
temperatures of the coolant fluid at the
condenser inlet and outlet.
vi)
For a carbon adsorption system such as a
fixed—bed adsorber that regenerates the
carbon bed directly onsite in the
control device, the design analysis must
consider the vent stream composition,
constituent concentrations,
flow rate,
relative humidity and temperature.
The
design analysis must also establish the
design exhaust vent stream organic
compound concentration level, number and
capacity of carbon beds, type and
working capacity of activated carbon
used for carbon beds, design total steam
flow over the period of each complete
carbon bed regeneration cycle, duration
of the carbon bed steaming and
cooling/drying cycles, design carbon bed
temperature after regeneration, design
carbon bed regeneration time and design
service life of carbon.
vii)
For a carbon adsorption system such as a
carbon canister that does not regenerate
the carbon bed directly onsite in the
control device, the design analysis must
consider the vent stream composition,
constituent concentrations,
flow rate,
relative humidity and temperature.
The
design analysis must also establish the
design outlet organic concentration
level, capacity of carbon bed, type and
working capacity of activated carbon
used for carbon bed and design carbon
replacement interval based on the total
carbon working capacity of the control
device and source operating schedule.
D)
A statement signed and dated by the owner or
operator certifying that the operating
128—615
146
parameters used in the design analysis
reasonably represent the conditions that
exist when the hazardous waste management
unit is or would be operating at the highest
load or capacity level reasonably expected to
occur.
E)
A statement signed and dated by the owner or
operator certifying that the control device
is designed to operate at an efficiency of
95
percent or greater unless the total organic
concentration limit of Section 724.932(a)
is
achieved at an efficiency less than 95 weight
percent or the total organic emission limits
of Section 724.932(a)
for affected process
vents at the facility are attained by a
control device involving vapor recovery at an
efficiency less than 95 weight percent.
A
statement provided by the control device
manufacturer or vendor certifying that the
control equipment meets the design
specifications’may be used to comply with
this requirement.
F)
Ifperformance tests are used to demonstrate
compliance, all test results.
c)
Design documentation and monitoring operating and
inspection information for each closed—vent system and
control device required to comply with the provisions
of this Part must be recorded and kept up-to-date in
the facility operating record.
The information must
include:
1)
Description and date of each modification that is
made to the closed—vent system or control device
design.
2)
Identification of operating parameter, description
of monitoring device, and diagram of monitoring
sensor location or locations used to comply with
Section 724.933(f) (1)
and
(2).
3)
Monitoring,
operating and inspection information
required by Section 724.933 (f) through
(k).
4)
Date, time and duration of each period that occurs
while the control device is operating when any
monitored parameter exceeds the value established
in the control device design analysis as specified
below:
128—616
147
A)
For a thermal vapor incinerator designed to
operate with a minimum residence time of 0.50
second at a minimum temperature of 760 C, any
period when the combustion temperature is
below 760 C.
B)
For a thermal vapor incinerator designed to
operate with an organic emission reduction
efficiency of 95 weight percent or greater,
any period when the combustion zone
temperature is more than 28 C below the
design average combustion zone temperature
established as a requirement of subsection
(b) (4) (C) (i).
C)
For a catalytic vapor incinerator, any period
when:
i)
Temperature
of
the
vent stream at the
catalyst bed inlet is more than 28 C
below the average temperature of the
inlet vent st’ream established as a
requirement of subsection
(b) (4) (C) (ii);
or
ii)
Temperature difference across the
catalyst bed is less than
80
percent
of
the design average temperature
difference established as a requirement
of subsection
(b) (4) (C) (ii).
D)
For a boiler or process heater, any period
when:
i)
Flame zone temperature
is more than 28
C
below the design average flame zone
temperature established as a requirement
of subsection
(b) (4) (C) (iii); or
ii)
Position changes where the vent stream
is introduced to the combustion zone
from the location established as a
requirement of subsection
(b) (4) (C) (iii).
E)
For a flare, period when the pilot flame is
not ignited.
F)
For a condenser that complies with Section
724.933(f) (2) (F) (i), any period when the
organic compound concentratidn level or
readings of organic compounds in the exhaust
128—6 17
148
vent stream from the condenser are more than
20 percent greater than the design outlet
organic compound concentration level
established as a requirement of subsection
(b) (4) (C) (v).
G)
For a condenser that complies with Section
724.933(f) (2) (F) (ii), any period when:
1)
Temperature of the exhaust vent stream
from the condenser is more than
6 C
above the design average exhaust vent
stream temperature established as a
requirement of subsection
(b) (4) (C) (v).
ii)
Temperature of the coolant fluid exiting
the condenser is more than
6 C above the
design average coolant fluid temperature
at the condenser outlet established as
a
requirement of subsection
(b) (4) ~C)(v).
H)
For a carbon adsorption system such as a
fixed—bed carbon adsorber that regenerates
the carbon bed directly onsite in the control
device and complies with Section
724.933(f) (2 ()G) (i), any period when the
organic compound concentration level or
readings of organic compounds in the exhaust
vent stream from the carbon bed are more than
20 percent greater than the design exhaust
vent stream organic compound concentration
level established as a requirement of
subsection
(b)(4) (C) (vi).
I)
For a carbon adsorption system such as a
fixed-bed carbon adsorber th’at regenerates
the carbon bed directly onsite in the control
device and complies with Section
724..933(f)(2)(G)(ii), any period when the
vent stream continues to flow through the
control device beyond the predetermined
carbon bed regeneration time established as a
requirement of subsection
(b) (4) (C) (vi).
5)
Explanation for each period recorded under
subsection
(C)
(4)
of the cause for control device
operating parameter exceeding the design value and
the measures implemented to correct the control
device operation.
6)
For a carbon adsorption system operated subject to
requirements specified in Section 724.933(g)
or
128—618
149
(h) (2), any date when existing carbon in the
control device is replaced with fresh carbon.
7)
For a carbon adsorption system operated subject to
requirements specified in Section 724.933(h) (1), a
log that records:
A)
Date and time when control device is
monitored for carbon breakthrough and the
monitoring device reading.
B)
Date when existing carbon in the control
device is replaced with fresh carbon.
8)
Date of each control device startup and shutdown.
d)
Records of the monitoring, operating and inspection
information required by subsections
(C)
(3) through
(8)
need be kept only 3 years.
e)
For a control device other than a thermal vapor
incinerator, catalytic vapor incinerator, flare,
boiler, process heater, condenser or carbon adsorption
system, the Agency shall specify the appropriate
recordkeeping ‘requirements.
f)
Up-to-date information and data used to determine
whether or not a process’ vent is subject to the
requirements in Section 724.932, including supporting
documentation as required by Section 724.934(d) (2),
when application of the knowledge of the nature of the
hazardous wastestreaxn or the process by which it was
produced is used, must be recorded in a ‘log that is.
kept in the facility operating record.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
128—6 19
150
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE
G:
WASTE
DISPOSAL
CHAPTER
I:
POLLUTION
CONTROL
BOARD
SUBCHAPTER
C:
HAZARDOUS
WASTE
OPERATING REQUIREMENTS
PART 725
INTERIM STATUS
STANDARDS
FOR
OWNERS
AND
OPERATORS OF
HAZARDOUS
WASTE TREATMENT, STORAGE
AND
DISPOSAL FACILITIES
SUBPART A:
GENERAL PROVISIONS
Purpose, Scope and Applicability
Imminent Hazard Action
SUBPART B:
GENERAL
FACILITY
STANDARDS
725.115
General Inspection Requirements
725.116
Personnel Training
725.117
General Requirements for Ignitable, Reactive or
Incompatible’ Wastes
725.118
Location Standards
SUBPART C:
PREPAREDNESS
AND
PREVENTION
Section
725.130
Applicability
725.131
Maintenance and Operation of Facility
725.132
Required Equipment
725.133
Testing
and
Maintenance
of
Equipment
725.134
Access to Communications or Alarm System
725.135
Required
Aisle
Space
725.137
Arrangements with Local Authorities
SUBPART D:
CONTINGENCY
PLAN AND
EMERGENCY PROCEDURES
Applicability
Purpose and Implementation of Contingency Plan
Content of Contingency Plan
Copies of Contingency Plan
Amendment of Contingency Plan
Emergency Coordinator
Emergency
Procedures
SUBPART E:
MANIFEST SYSTEM, RECORDKEEPING
AND
REPORTING
Applicability
Use of Manifest System
Manifest
Discrepancies
Section
725.101
725.104
Sect ion
725.110
725. 111
725.112
725.113
725. 114
Applicability
USEPA
Identification
Number
Required
Notices
General
Waste
Analysis
Security
Sect ion
725. 150
725. 151
725.152
725. 153
725. 154
725.155
725. 156
Section
725. 170
725.171
725. 172
128—620
151
725.173
Operating Record
725.174
Availability, Retention and Disposition of Records
725.175
Annual Report
725.176
Unmanifested Waste Report
725.177
Additional’ Reports
SUBPART
F:
GROUNDWATER MONITORING
Section
725. 190
Applicability
725.191
Groundwater Monitoring System
725.192
Sampling and Analysis
725.193
Preparation,
Evaluation
and
Response
725.194
Recordkeeping
and
Reporting
SUBPART
G:
CLOSURE
AND
POST-CLOSURE
Section
725.210
Applicability
725.211
Closure Performance Standard
725.212
Closure Plan; Amendment of Plan
725.213
Closure; Time Allowed for Closure
725.214
Disposal or Decontamination of Equipment, Structures
and Soils
725.215
Certification of Closure
725.216
Survey Plat
725.217
Post-closure~Careand Use of Property
725.218
Post-closure Plan; Amendment of Plan
725.219
Post-Closure Notices
725.220
Certification of Completion of Post-Closure Care
SUBPART
H:
FINANCIAL
REQUIREMENTS
Section
725.240
Applicability
725.241
Definitions of Terms as Used in this Subpart
725.242
Cost Estimate for ‘Closure
725.243
Financial Assurance for Closure
725.244
Cost Estimate ~or Post-closure Care
725.245
Financial Assurance for Post—closure Monitoring and
Maintenance
725.246
Use of a Mechanism for Financial Assurance of Both
Closure and Post—closure Care
725.247
Liability Requirements
725.248
Incapacity of Owners or Operators, Guarantors or
Financial Institutions
725.251
Promulgation of Forms (Repealed)
SUBPART I:
USE
AND
MANAGEMENT OF CONTAINERS
Section
725.270
Applicability
725.271
Condition of Containers
725.272
Compatibility of Waste with Container
725.273
Management of Containers
725.274
Inspections
128—62 1
152
725.276
725
•
277
Section
725. 290
725~291
725. 292
725.293
725. 294
725. 295
725. 296
725.297
725. 298
725. 299
725. 300
725.301
Section
725. 320
725.321
725.322
725. 323
725.325
725.326
725. 328
725. 329
725. 330
Section
725.350
725. 351
725. 352
725.353
725. 354
725. 356
7 25.357
725. 358
Section
725.370
725. 372
725.373
725.376
725. 378
725. 379
725. 380
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
SUBPART
J:
TANK
SYSTEMS
Applicability
Assessment of Existing
Tank
System’s Integrity
Design and Installation of New Tank Systems or
Components
Containment and Detection of Releases
General Operating Requirements
Inspections
Response to leaks or spills and disposition of Tank
Systems
Closure and Post-Closure Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for. Incompatible Wastes
Waste
Analysis and Trial Tests
Generators
of
100
to
1000 kg/mo.
SUBPART
K:
SURFACE
IMPOUNDMENTS
Applicability
Design
Requirements
General Operating Requirements
Containment
System
Waste
Analysis
and
Trial
Tests
Inspections
Closure and Post—Closure Care
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
SUBPART L:
WASTE PILES
Applicability
Protection from Wind
Waste Analysis
Containment
Design Requirements
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Closure and Post-Closure Care
SUBPART M:
LAND
TREATMENT
Applicability
General Operating Requirements
Waste Analysis
Food Chain Crops
Unsaturated Zone (Zone of Aeration) Monitoring
Recordkeeping
Closure and Post-closure
128—622
153
725.381
Special Requirements for Ignitable or Reactive Waste
725.382
Special Requirements for Incompatible Wastes
SUBPART N:
LANDFILLS
Section
725.400
725.401
725.402
725.409
725.410
725.412
725.413
725.
414
725.
415
725.416
Applicability
Design Requirements
General Operating Requirements
Surveying and Recordkeeping
Closure and Post—Closure
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
Special Requirements for Liquid Wastes
Special Requirements for Containers
Disposal of Small Containers of Hazardous Waste in
Overpacked Drums
(Lab Packs)
SUBPART
0:
INCINERATORS
Applicability
Waste Analysis
General Operating Requirements
Monitoring and Inspection
Closure
Interim Status Incinerators Burning Particular
Hazardous Wastes
SUBPART P:
THERMAL TREATMENT
Other
Thermal
Treatment
General Operating Requirements
Waste
Analysis
Monitoring and Inspections
Closure
Open Burning; Waste Explosives
Interim Status Thermal Treatment Devices Burning
Particular Hazardous Waste
SUBPART
Q:
CHEMICAL,
PHYSICAL AND BIOLOGICAL TREATMENT
Applicabi 1i.ty
General Operating Requirements
Waste Analysis and Trial Tests
Inspections
Closure
Special Requirements for Ignitable or Reactive Waste
Special Requirements for Incompatible Wastes
SUBPART R:
UNDERGROUND INJECTION
Section
725.530
Applicability
Section
725.440
725.
441
725. 445
725.
447
725. 451
725.452
Section
725.
470
725.473
725. 475
725.
477
725.481
725.
482
725.
483
Section
725.
500
725.
501
725. 502
725.503
725.
504
725. 505
725. 506
128—623
154
SUBPART
W:
DRIP PADS
Section
725. 540
725.541
725.542
725.543
725.544
725.545
Section
725.930
725.931
725.932
725. 933
725. 934
725. 935
Section
725.950
725. 951
725. 952
‘725. 953
725. 954
725. 955
725.956
725.
957
725.958
725.959
725.960
725.961
725.
962
725. 963
725. 964
Applicability
Assessment
of
existing drip pad integrity
Design and installation of new drip pads
Design
and operating requirements
Inspections
Closure
S~UBPART
AA:
AIR EMISSION STANDARDS FOR PROCESS VENTS
Appendix A
Appendix B
Appendix C
Appendix D
Appendix E
Applicability
Definitions
Standards:
Process Vents
Standards:
Closed—vent Systems and Control Devices
Test
methods
and
procedures
Recordkeeping Requirements
Applicability
Definitions
Standards:
Standards:
Standards:
Service
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the Environmental Protection Act (Ill. Rev.
Stat.
1989,
ch.
111—1/2, pars.
1022.4 and 1027).
SOURCE:
Adopted
in R81—22,
43 PCB 427, at 5
Ill.
Reg. 9781,
effective as noted in 35
Ill. Ada. Code 700.106; amended and
codified in R81—22,
45 PCB 317, at
6 Iii. Reg.
4828, effective as
noted in 35 Ill.
Adm. Code 700.106; amended in R82-18,
51 PCB
SUBPART
BB:
AIR
EMISSION
STANDARDS
FOR
EQUIPMENT
LEAKS
Pumps in Light Liquid Service
Compressors
Pressure Relief Devices in Gas/Vapor
Standards:
Sampling Connecting Systems
Standards:
Open—ended Valves or Lines
Standards:
Valves in Gas/Vapor or Light Liquid Service
Standards:
Pumps, Valves, Pressure Relief Devices,
Flanges and Other Connectors
Standards:
Delay of Repair
Standards:
Closed—vent Systems and Control Devices
Percent Leakage Alternative for Valves
Skip Period Alternative for Valves
Test Methods and Procedures
Recordkeeping Requirements
Recordkeeping Instructions
EPA
Report
Form
and Instructions
(Repealed)
EPA Interim Primary Drinking Water Standards
Tests for Significance
Examples of Potentially Incompatible Waste
128—624
155
831, at
7 Ill.
Reg. 2518, effective February 22,
1983;
amended
in
R82—19,
53 PCB 131, at
7 Ill. Reg.
14034, effective October
12,
1983;
amended
in
R84-9, at 9 Ill.
Reg. 11869, effective July 24,
1985; amended in R85-22 at 10
Ill. Reg.
1085, effective January
2,
1986;
amended in R86—1 at 10 Ill. Reg. 14069, effective August
12,
1986; amended in R86—28 at 11 Ill.
Reg.
6044, effective March
24,
1987; amended in R86—46 at 11
Ill. Reg.
13489, effective
August
4,
1987; amended in R87—5 at 11 Ill. Reg.
19338, effective
November 10,
1987; amended in R87-26 at 12
Ill. Reg.
2485,
effecti,ve
January
15,
1988; amended inR87-39 at
12
Ill. Reg.
13027,
effective July 29,
1988; amended in
R88—16
at
13
Ill.
Reg.
437, effective December 28,
1988;
amended
in
R89—1
at
13
Ill.
Reg.
18354, effective November 13,
1989; amended in R90-2
at 14
Ill.
Reg.
14447, effective August 22,
1990; amended in R90—10 at
14 Ill. Reg.
16498, effective September 25,
1990; amended in R90-
11 at 15 Ill. Reg.
9398, effective June 17,
1991; amended in R91-
1 at 15 Ill.
Reg. 14534, effective October 1,
1991;
amended in
R91—13 at 16 Ill.
Reg.
,
effective
SUBPART B:
GENERAL FACILITY STANDARDS
Section 725.113
General Waste Analysis
a)
Waste analysis:
1)
Before an owner or operator treats,
stores or
disposes of any hazardous waste,
or non—hazardous
waste if applicable under Section 725.213(d), the
owner or operator shall obtain a detailed chemical
and physical analysis of a representative sample
of the waste.
At a minimum, this analysis must
contain all the information which must be known to
treat, store or dispose of the waste in accordance
with the requirements of this Part and 35 Ill.
Adin. Code 728.
2)
The analysis may include data developed under 35
Ill. Adm. Code 721 and existing published or
documented data on the hazardous waste or on waste
generated from similar processes.
BOARD
NOTE:
For
example,
the
facility’s
record
of
analyses performed on the waste before the
effective date of these regulations or studies
conducted on hazardous waste generated from
processes similar to that which generated the
waste to be managed at the facility may be
included in the data base
required
to
comply
with
subsection
(a) (1), except as otherwise specified
in 35 Ill. Ada. Code 728.107(b)
and
(c).
The
owner or operator of an off—site facility may
arrange for the generator of the hazardous waste
128—625
156
to supply part or all of the information required
by subsection
(a)(1).
If the generator does not
supply the information and the owner or operator
chooses to accept a hazardous waste, the owner or
operator is responsible for obtaining the
information required to comply with this Section.
3)
The analysis must be repeated as necessary to
ensure that it is accurate and up to date.
At a
minimum, the analysis must be repeated:
A)
When the owner or operator is notified, or
has reason to believe, that the process or
operation generating the hazardous waste, or
non—hazardous waste if applicable under
Section 725.213(d), has changed; and
B)
For off—site facilities, when the results of
the inspection required in subsection
(a)(4)
indicate that the hazardous waste received at
the facility does not match the ‘waste
designated on the accompanying manifest or
shipping paper.
4)
The owner’ or operator of an off-site facility
shall inspect and, if necessary,
analyze each
hazardous waste movement received at the facility
to determine whether it matches the identity of
the waste specified on the accompanying manifest
or shipping paper.
b)
The owner or operator shall develop and follow a
written waste analysis plan which describes the
procedures which the owner or operator will carry out
to comply with subsection
(a).
The owner or operator
shall keep this plan at the facility.
At a minimum,
the plan must specify:
1)
The parameters for which each hazardous waste, or
non—hazardous waste if applicable under Section
725.213(d), will be analyzed and the rationale for
the selection of these parameters
(i.e., how
analysis for these parameters will provide
sufficient information on the waste’s properties
to comply with subsection
(a).
2)
The test methods which will be used to test for
these parameters.
3)
The sampling method which will be used to obtain a
representative sample of the waste to be analyzed.
A representative sample may be obtained using
128—626
157
either:
A)
One of the sampling methods described in 35
Ill. Ada. Code 721.Appendix A or
B)
An equivalent sampling method.
BOARD NOTE:
See 35 Ill. Adm. Code 720.120(c)
for related discussion.
4)
The frequency with which the initial analysis of
the waste will be reviewed or repeated to ensure
that the analysis is accurate and up—to-date.
5)
For off—site facilities, the waste analyses that
hazardous waste generators have agreed to supply.
6)
Where applicable, the methods which will be used
to
meet
the additional waste analysis requirements
for specific waste management methods ‘as specified
in
Sections
725.293725.300,
725.325,
725.352,
725.373,
725.414,
725.441,
725.475,
725.502,
725.934(d)
and 725.963(d), and 35
Ill.
Adm.
Code
728.107.
And,
7)
For surface impoundaents exempted from land
disposal restrictions under 35 Ill.
Ada. Code
728.104(a),
the procedures and schedules for:
A)
The sampling of impoundment contents;
B)
The analysis of test data;
and,
C)
The annual removal of residues which are not
delisted under 35 Ill. Adm. Code
720.122
or
which exhibit a characteristic of hazardous
waste,
and either:
i)
Do not meet applicable treatment
standards of 35 Ill.
Adm. Code
728.Subpart D; or
ii)
Where no treatment standards have been
established:
Such residues are
prohibited from land disposal under 35
Ill. Ada. Code 728.132 or 728.139;
or
such residues are prohibited from land
disposal under 35 Ill. Adm. Code
728.133(f).
c)
For off-site facilities, the waste analysis plan
required in subsection
(b) must also specify the
128—627
158
procedures which will be used to inspect and,
if
necessary,
analyze each movement of hazardous waste
received at the facility to ensure that it matches the
identity of the waste designated on the accompanying
manifest or shipping paper.
At a minimum, the plan
must describe:
1)
The procedures which will be used to determine the
identity of each movement of waste managed at the
facility; and
2)
The sampling method which will be used to obtain a
representative sample of the waste to be
identified,
if the identification method includes
sampling.
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
Section 725.173
Operating Record
a)
The owner or operator shall keep a written operating
record
at
the
facility.
b)
The following information must be recorded as it
becomes available and maintained in the operating
record until closure of the facility.
1)
A description and the quantity of each hazardous
waste received and the method or methods and date
or
dates
of
its
treatment,
storage or disposal at
the facility as required by Appendix A;
2)
The location of each hazardous waste within the
facility and the quantity at each location.
For
disposal facilities the location and quantity of
each hazardous waste must be recorded on a map or
diagram of each cell or disposal area.
For all
facilities this information must include cross-
references to specific manifest document numbers
if the waste was accompanied by a manifest;
BOARD NOTE:
See Sections 725.219,
725.379 and
725.409 for related requirements.
3)
Records and results of waste analysis and trial
tests performed as specified in Sections 725.113,
725.293725.300,
725.325, 725.352,
725.373,
725.414,
725.441’, 725.475,
725.502, 725.934 and
725.963 and 35 Ill. Adm. Code 728.104(a)
and
728.107;
128—628
159
4)
Summary reports and details of all incidents that
require implementing the contingency plan as
specified in Section 725.156(j);
5)
Records and results of inspections as required by
Sections 725.115(d)
(except these data need be
kept only three years);
6)
Monitoring, testing or analytical data where
required by Sections 725.190, 725.194, 725.291,
725.293, 725.295, 725.376, 725.378, 725.380(d) (1),
725.447,
725.477,
725.934(c) through
(f),
725.935, 725.963(d) through
(i) and 725.964;
BOARD NOTE:
As required by Section 725.194,
monitoring data at disposal facilities must be
kept throughout the post-closure period.
7)
All closure cost estimates under Section 725.242
and, for disposal facilities,
all post-closure
cost estimates under Section 725.244;
8)
Records of the quantities (and date of placement)
for each shipment of hazardous waste placed in
land disposal units under an extension of the
effective date of any land disposal restriction
granted pursuant to 35 Ill.
Ada. Code 728.105,
a
petition pursuant to 35 Ill. Ada. Code 728.106 or
a certification under 35 Ill. Ada. Code 728.108,
and the applicable notice required of a generator
under 35 Ill. Adm. Code 728.107(a);
9)
For an off—site treatment facility,
a copy of the
notice, and the certification and demonstration,
if applicable, required of the generator or the
owner or operator under 35 Ill. Adm. Code 728.107
or 728.108;
10)
For an on—site treatment facility, the information
contained in the notice
(except the manifest
number), and the certification and demonstration,
if applicable,
required of the generator or the
owner or operator under 35 Iii. Adm. Code 728.107
or 728.108;
11)
For an off—site land disposal facility,
a copy of
the notice, and the certification and
demonstration,
if applicable, required of the
generator or the owner or operator of a treatment
facility under 35 Ill. Ada. Code 728.107 or
728.108, whichever is applicable; and
128—629
160
12)
For an on-site land disposal facility, the
information contained in the notice required of
the generator or
owner
or operator of a treatment
facility under 35
Ill. Ada. Code 728.107,
except
for the manifest
number,
and the certification and
demonstration,
if applicable, required under 35
Ill. Ada. Code 728.108, whichever is applicable.
13)
For an off—site storage facility,
a copy of the
notice, and the certification and demonstration if
applicable, required of the generator or the owner
or operator under 35 Ill. Ada. Code 728.107 or
728.108;
and,
14)
For an on-site storage facility, the information
contained in the notice
(except the manifest
number), and the certification and demonstration
if applicable, required of the generator or the
owner or operator under 35 Ill.
Ada. Code 728.107
or 728.108.
(Source:
Amended
at 16 Ill. Reg.
,
effective
)
Section 725.212
Closure Plan;
Amendment
of Plan
a)
Written Plan.
Within six months after the effective
date of the rule that first sublects a facility to
provisions of this Section. tPhe owner or operator of a
hazardous waste management facility shall have a
written closure plan.
Until final closure
is completed
and certified in accordance with Section 725.215,
a
copy of the most current plan must be furnished to the
Agency upon request including request by mail.
In
addition, for facilities without approved plans,
it
must also be provided during site inspections on the
day of inspection to any officer, employee or
representative of the Agency.
b)
Content of plan.
The plan must identify the steps
necessary to perform partial or final closure of the
facility at any point during its active life.
The
closure plan must include, at least:
1)
A description of how each hazardous waste
management unit at the facility will be closed in
accordance with Section 725.211; and
2)
A description of how final closure of the facility
will be conducted in accordance with Section
725.211. The description must identify the maximum
extent of the operation which will be unclosed
128—630
161
during the active life of the facility and
3)
An estimate of the maximum inventory of hazardous
wastes ever on—site over the active life of the
facility and
a detailed description of the methods
to be used during partial and final closure,
including, but not limited to methods for
removing, transporting, treating, storing or
disposing of all hazardous waste,
and
identification of and the type(s)
of off—site
hazardous waste management unit(s) to be used,
if
applicable; and
4)
A detailed description of the steps needed to
remove or decontaminate all hazardous waste
residues and contaminated containment system
components, equipment,
structures and soils during
partial and final closure including, but not
limited to, procedures for cleaning equipment and
removing contaminated soils, methods for sampling
and testing surrounding soils and criteria for
determining the extent of decontamination
necessary to satisfy the closure performance
standard; and
5)
A detailed description of other activities
necessary during the partial and final closure
period to ensure that all partial closures and
final closure satisfy the closure performance
standards,
including, but not limited to,
groundwater monitoring,
leachate collection,
and
run-on and run—off control; and
6)
A schedule for closure of each hazardous waste
management unit and for final closure of the
facility.
The schedule must include, at a
minimum, the total time required to close each
hazardous waste management unit and the time
required for intervening closure activities which
will allow tracking of the progress of partial and
final closure.
(For example,
in the case Qf a
landfill unit,
estimates of the time required to
treat or dispose of all hazardous waste inventory
and of the time required to place a final cover
must be included.); and
7)
An estimate of the expected year of final closure
for facilities that use trust funds to demonstrate
financial assurance under Sections 725.243 or
725.245 and whose remaining operating life is less
than twenty years, and for facilities without
approved closure plans.
128—63 1
162
c)
Amendment of plan.
The owner or operator may amend the
closure plan at any time prior to the notification of
partial or final closure of the facility.
An owner or
operator with an approved closure plan shall submit a
written
request to the Agency to authorize a change to
the approved closure plan.
The written request must
include a copy of the amended closure plan for approval
by the Agency.
1)
The owner or operator shall amend the closure
plan, whenever:
A)
Changes in the operating plans or facility
design affect the closure plan,
or
B)
Whenever there is a change in the expected
year of closure, if applicable, or
C)
In conducting partial or final closure
activities, unexpected events require a
modification of the closure plan.
2)
The owner or operator shall amend the closure plan
at least 60 days prior to the proposed change in
facility design or operation,
or no later than 60
days after an unexpected event has occurred which
has affected the closure plan.
If an unexpected
event occurs during the partial or final closure
period, the owner or operator shall amend the
closure plan no later than 30 days after the
unexpected event.
These provisions also apply to
owners or operators of surface impoundments and
waste piles who intended to remove all hazardous
wastes at closure, but are required to close as
landfills in accordance with Section 725.410.
3)
An owner or operator with an approved closure plan
shall submit the modified plan to the Agency at
least 60 days prior to the proposed change in
facility design or operation,
or no more than 60
days after an unexpected event has occurred which
has affected the closure plan.
If an unexpected
event has occurred during the partial or final
closure period, the owner or operator shall submit
the modified plan no more than 30 days after the
unexpected event.
These provisions also apply to
owners or operators of surface impoundments and
waste piles who intended to remove all hazardous
wastes at closure but are required to close as
landfills in accordance with Section 725.410.
If
the amendment to the plan is a Class
2 or
3
128—632
163
modification according to the criteria
in 35 Ill.
Adm. Code 702.280, the modification to the plan
shall be approved according to the procedures in
subsection
(d) (4).
4)
The Agency may request modifications to the plan
under the conditions described in subsection
(c) (1).
An owner or operator with an approved
closure plan shall submit the modified plan within
60 days of the request from the Agency, or within
30 days if
the
unexpected event occurs during
partial or final closure.
If the amendment is
considered a Class
2 or 3 modification according
to the criteria in 35 Ill. Adm. Code 702.280, the
modification to the plan must be approved in
accordance with the procedures in subsection
(d) (4).
d)
Notification of partial closure and final closure.
1)
When notice is required.
~j
The owner or operator shall submit the
closure plan to the Agency at least 180 days
prior to the date on’ which the owner or
operator expects to begin closure of the
first surface impoundment, waste pile,
land
treatment or landfill unit,
or final closure
of a facility withif it involves such a unit~
whichever is earlier.
~j.
The owner or operator shall submit the
closure plan to the Agency at least 45 daYs
prior to the date on which the owner or
oDerator exPects to begin partial or final
closure of
a boiler or industrial furnace.
Q1
The owner or operator shall submit the
closure plan to the Agency at least 45 days
prior to the date on which the owner or
operator expects to begin final closure of a
facility with only tanks, container storage
or incinerator units.
Qj
Owners or operators with approved closure
plans shall notify the Agency in writing at
least 60 days prior to the date on which the
owner or operator expects to begin closure of
a surface impoundment, waste pile,
landfill
or land treatment unit,
or final closure of a
facility involving such a unit.
128—633
164
~
Owners or operators with approved closure
plans shall notify the Agency in writing at
least 45 days Prior to the date on which the
owner or operator expects to begin partial or
final closure of a boiler or industrial
L~rnace.
fi
Owners and operators with approved closure
plans shall notify the Agency in writing at
least 45 days prior to the date on which the
owner or operator expects to begin final
closure of a facility with only tanks,
container storage or incinerator units.
2)
The date when the owner or operator “expects to
begin closure” must be either:
A)
w~ithin30 days after the date on which any
hazardous waste management unit receives’ the
known final volume of hazardous wastes or,
if
there is a reasonable possibility that the
hazardous waste management unit will receive
additional hazardous wastes, no later than
one year after the date on which the unit
received the most recent volume of hazardous
waste.
If the owner or operator of a
hazardous waste management unit demonstrates
to the Agency that the hazardous waste
management unit or facility has the capacity
to receive additional hazardous wastes’ and
that the owner or operator has taken and will
continue to take, all steps to prevent
threats to human health and the environment,
including compliance with all interim status
requirements, the Agency shall approve an
extension to this one—year limit; or
B)
For units meeting the requirements of Section
725.213(d), no later than 30 days after the
date on which the hazardous waste management
unit receives’ the final known final volume of
non—hazardous wastes,
or,
if there is a
reasonable possibility that the hazardous
waste managernent unit will receive additional
non—hazardous wastes, no later than one year
after the date on which the unit received the
most recent volume of non—hazardous wastes.
If the owner
or. operator demonstrates to
the
Agency that the hazardous waste management
unit has the capacity to receive additional
non—hazardous wastes and that the owner and
operator have taken, and will continue to
128—634
165
take,
all steps to prevent threats to human
health and the environment, including
compliance with all applicable interim status
requirements, the Agency shall approve an
extension to this one—year limit.
3)
The owner or operator shall submit the closure
plan to the Agency no later than 15 days after:
A)
Termination of interim status (except when a
permit is issued to the facility
simultaneously with termination of interim
status); or
B)
Issuance of a judicial decree or Board order
to cease receiving hazardous wastes or close.,
4)
The Agency shall provide the owner or operator and
the public, through a newspaper notice, the
opportunity to submit written comments on~theplan
and request modifications of the plan no later
than 30 days from the date of the notice.
The
Agency shall also,
in response to a request or at
its own discretion, hold a public hearing whenever
such a hearing might clarify one or more issues
concerning
a closure plan.
The Agency shall give
public notice of the hearing at least 30 days
(Public notice of the hearing
before it occurs.
may be given at the same time as notice of the
opportunity for the public to submit written
comments
and the two notices may be combined.)
The Agency shall approve, modify or disapprove the
plan within 90 days of its receipt.
If the Agency
does not approve the plan, the Agency shall
provide the owner or operator with a detailed
written statement of reasons for the refusal, and
the owner or operator shall modify the plan or
submit a new plan for approval within 30 days
after receiving such written statement.
The
Agency shall approve or modify this plan in
writing within 60 days.
If the Agency modifies
the plan, this modified plan becomes the approved
closure plan.
The Agency shall assure that the
approved plan is consistent with Sections 725.211
through 725.215 and the applicable requirements of
Sections 725.190 et seq.,
725.297, 725.328,
725.358, 725.380, 725.410,
725.451, 725.481 and
725.504.
A copy of this modified plan with a
detailed statement of reasons for the
modifications must be mailed to the owner or
operator.
128—635
166
e)
Removal of wastes and decontamination or dismantling of
equipment.
Nothing in this Section precludes the owner
or operator from removing hazardous wastes and
decontaminating or dismantling equipment in accordance
with the approved partial or final closure plan at any
time before or after notification of partial or
final
closure.
(Source:
Amended at 16
Ill. Reg.
,
effective
)
Section 725.213
Closure; Time Allowed for Closure
a)
Within 90 days after receiving the final volume of
hazardous wastes, or the final volume of non—hazardous
wastes,
if the owner or operator complies with all the
applicable requirements of subsections
(d) and
(e), at
a hazardous waste management unit or facility,
or 90
days after approval of the closure plan, whichever’ is
later, the owner or operator shall treat,
remove from
the unit or facility or dispose of on—site, all
hazardous wastes in accordance with the approved
closure plan.
The Agency shall approve a longer period
if the owner or operator demonstrates that:
1)
Either:
A)
The activities required to comply with this
paragraph will,
of necessity,
take longer
than 90 days to complete; or
B)
All of the following:
i)
The hazardous waste management unit or
facility has the capacity to receive
additional hazardous wastes, or has the
capacity to receive non—hazardous
wastes,
if the owner or operator
complies with subsections
(d) and (e);
ii)
There is a reasonable likelihood that
the
owner
or operator, or another person
will recommence operation of’ the
hazardous waste manaqement unit or
facility within one year; and
iii) Closure of the hazardous waste
management unit or facility would be
incompatible with continued operation of
the site; and
2)
The owner or operator have taken and will continue
128—636
167
to take ~ll steps to prevent threats to human
health and the environment including compliance
with all applicable interim status requirements.
b)
The owner or operator shall complete partial and final
closure activities in accordance with the approved
closure plan and within 180 days after receiving the
final volume of hazardous wastes, or the final volume
of non—hazardous wastes,
if the owner or operator
complies with all the applicable requirements of
subsections
(d) and
(e), at the hazardous waste
management unit or facility, or 180 days after approval
of the closure plan,
if that is later.
The Agency
shall approve an extension to the closure period if the
owner or operator demonstrates that:
1)
Either:
A)
The partial or final closure activities will,
of necessity, take longer than 180 days to
complete; or
B)
All of the following:
i)
The hazardous waste management unit or
facility has the capacity to receive
additional hazardous wastes, or ‘the
final volume of non—hazardous wastes,
if
the owner or operator complies with all
the applicable requirements of
subsections
(d) and
(e); and
ii)
There is a reasonable likelihood that
the owner or operator or another person
will recommence operation of the
hazardous waste management unit or
facility within one year; and
iii) Closure of the hazardous waste
management unit or facility would be
incompatible with continued operation of
the site; and
2)
The owner and operator have taken and will
continue to take all steps to prevent threats to
human health and the environment from the unclosed
but not operating hazardous waste management unit
or facility, including compliance with all
applicable interim status requirements.
c)
The demonstration referred to in subsections
(a) (1) and
(b) (1) must be made as follows:
128—637
168
1)
The demonstration in subsection
(a) (1) must be
made at least 30 days prior to the expiration of
the 90-day period in subsection (a); and
2)
The demonstrations in subsection
(b) (1) must be
made at least 30 days prior to the expiration of
the 180-day period in subsection
(b), unless the
owner or opertaor is otherwise subject to
deadlines in subsection
(d).
d)
Continued receipt of non—hazardous waste.
The Agency
shall permit an owner or operator to receive
non—hazardous wastes in a landfill,
land treatment unit
or surface impoundment unit after the final receipt of
hazardous wastes at that unit
if:
1)
The owner or operator submits an amended Part B
application, or a new Part B application
if
nOne
was previously submitted, and demonstrates that:
A)
The unit has the existing design capacity as
indicated on the Part A application to
receive non—hazardous wastes; and
B)
There is a reasonable likelihood that the
owner or operator or another person will
receive non—hazardous waste in the unit
within one year after the final receipt of
hazardous wastes; and
C)
The non—hazardous wastes will not be
incompatible with any remaining wastes
in the
unit,
or with the facility design and
operating requirements of the unit or
facility under this Part; and
D)
Closure of the hazardous waste management
unit ~wouldbe incompatible with continued
operation of the unit or facility; and
E)
The owner or operator is operating and will
continue to operate in compliance with all
applicable interim status requirements; and
2)
The Part B application includes an amended waste
analysis plan, groundwater monitoring and response
program, human exposure assessment required under
35 Ill. Ada. Code 703.186 and closure and
post-closure plans and updated cost estimates and
demonstrations of financial assurance for closure
and post—closure care as necessary and
128—638
169
appropriate, to reflect any changes due to the
presence of hazardous constituents in the
non—hazardous wastes, and changes in closure
activities, including the expected year of closure
if applicable under Section 725.212(b) (7), as a
result of the receipt of non—hazardous wastes
following the final receipt of hazardous wastes;
and
3)
The Part B application is amended, as necessary
and appropriate, to account for the receipt of
non—hazardous wastes following receipt of the
final volume of hazardous wastes; and
4)
The Part B application and the demonstrations
referred to in subsections
(d) (1) and
(2) are
submitted to the Agency no later than 180 days
prior to the date on which the owner or operator
of the facility receives the known final volume of
hazardous wastes,
or no later than 90~daysafter
the effective date of this Section, whichever is
later.
e)
Surface impoundments.
In addition to the requirements
in subsection
(d), an owner or’ operator of a hazardous
waste surface impoundment which is not in compliance
with the liner and leachate collection system
requirements in Section 725.321(a)
shall receive
non—hazardous wastes
only, as authorized by an adjusted
standard pursuant to this subsection.
1)
The petition for adjusted standard must include:
A)
A plan for removing hazardous wastes; and
B)
A contingent corrective measures plan.
2)
The removal plan must provide for:
A)
Removing all hazardous liquids; and
B)
Removing all hazardous sludges to the extent
practicable without impairing the integrity
of the liner or liners,
if any; and
C)
Removal of hazardous wastes no later than 90
days after the final receipt of hazardous
wastes.
The Board will allow a longer time,
if the owner or operator demonstrates:
i)
That the removal of hazardous wastes
will, of necessity, take longer than the
128—639
170
alloted period to complete; and
ii)
That an extension will not pose a threat
to human health and the environment.
3)
The contingent corrective measures plan:
A)
Must meet the requirements of a corrective
action plan under Section 724.199, based upon
the assumption that a release has been
detected from the unit.
B)
May be a portion of a corrective action plan
previously submitted under Section 724.199.
C)
May provide for continued receipt of
non—hazardous wastes at the unit following a
release only if the owner or operator
demonstrates that continued receipt of wastes
will not impede’ corrective action.
D)
Must provide for implementation within one
year after a release,
or within one year
after the grant of the adjusted standard,
whichever is later.
4)
Release.
A release is a statistically significant
increase
(or decrease in the case of pH)
in
hazardous constituents over background levels,
detected in accordance with the requirements in
Subpart
F.
5)
In the event of a release, the owner or operator
of the unit:
A)
Within 35 days, file with the Board a
petition for adjusted standard.
If the Board
finds that it is necessary to do so in order
to protect human health and the environment,
the Board will modify the adjusted standard
to require the owner or operator to:
i)
Begin to implement the corrective
measures plan in less than one year;
or,
ii)
Cease the receipt of wastes until the
plan has been implemented.
iii) The Board will retain jurisdiction or
condition the adjusted standard so as to
require the filing of a’new petition to
address any required closure pursuant to
128—640
171
subsection
(e) (7).
B)
Shall implement the contingent corrective
measures plan.
C)
May continue to receive wastes at the unit if
authorized by the approved contingent
measures plan.
6)
Semi-annual report.
During the period of
corrective action, the owner or operator shall
provide semi—annual reports to the Agency which:
A)
Describe the progress of the corrective
action program;
B)
Compile all groundwater monitoring data; and
C)
Evaluate the effect of the continued receipt
of non-hazardous wastes on the effectiveness
of the corrective action.
7)
Required closure.
The owner or operator shall
commence closure of the unit in accordance with
the closure plan and the requirements of this Part
if the Board terminates the adjusted standard, or
if the adjusted standard terminates pursuant to
its terms.
A)
The Board will terminate the adjusted
standard if the owner or operator failed to
implement corrective action measures in
accordance with the approved contingent
corrective measures plan; or
B)
The Board will terminate the adjusted
standard if the owner or operator fails to
make substantial progress in implementing the
corrective measures plan and achieving the
facility’s groundwater protection standard,
or background levels if the facility has not
yet established a groundwater protection
standard; or
C)
The adjusted standard will automatically
terminate if the owner or operator fails to
implement the removal plan.
D)
The adjusted standard will automatically
terminate if the owner or operator fails to
timely file a required petition for adjusted
standard.
128—64 1
172
8)
Adjusted standard procedures.
The following
procedures must be used in granting, modifying c
terminating an adjusted standard pursuant to
thi.
subsection.
A)
Except as otherwise provided, the owner or
operator shall follow the procedures of 35
Ill. Adm. Code 106.Subpart G to petition th
Board £or an adjusted standard.
B)
Initial justification.
The Board will gran~
an adjusted standard pursuant to subsection
(e) (1)
if
the
owner or operator demonstrates
that the removal plan and contingent
corrective measures plans meet the
requirements of subsections
(e) (2)
and
(3).
C)
The Board will include the following
conditions in granting an adjusted standard
pursuant to subsection
(e) (1):
i)
A plan for removing hazardous wastes.
ii)
A requirement that the owner or operato
remove hazardous wastes in accordance
with the plan.
iii) A contingent corrective measures plan.
iv)
A requirement that,
in the event of a
release, the owner or operator shall:
within 35 days,
fil’e with the Board a
petition for adjusted standard;
implement the corrective measures plan;
and,
file semi—annual reports with the
Agency.
v)
A condition that the adjusted standard
will terminate if the owner or operator
fails to:
implement the removal plan;
or, timely file a required petition for
adjusted standard.
vi)
A requirement that,
in the event the
adjusted standard is terminated, the
owner or operator shall commence closure
of the unit in accordance with the
requirements of the closure plan and
this Part.
D)
Justification in the event of a release.
The
128—642
173
Board will modify or terminate the adjusted
standard pursuant to a petition filed under
subsection
(e) (5) (A) as provided in that
subsection or in subsection
(e) (7).
9)
The owner or operator may file a revised closure
plan within 15 days after an adjusted standard is
terminated.
(Source.:
Amended at 16 Ill. Reg.
)
,
effective
SUBPART 0:
INCINERATORS
Section 725.440
a)
Applicability
r~i—r~—r’~i—~~
hn~—ri
1n~n,—ni~
wastes
1
boilers or in industrial furnaces in order to
destroy them,
or who burn hazardou3 waste in
boilers or in industrial furnaces for any
recycling purp
“
-
this Cubpart.
b)
Owners and operators of incinerators burning hazardous
waste are exempt from all of the requirements of this
Subpart, except Section 725.451
(Closure), provided
that the owner or operator has documented,
in writing,
that the waste would not reasonably be expected to
contain any of the hazardous constituents listed in 35
Ill. Adm. Code 721.Appendix H, and such document~ation
is retained at the facility,
if the waste to be burned
is:
1)
Listed as a hazardous waste in 35 Ill. Ada. Code
721.Subpart D, solely because it is ignitable
(Hazard Code I), corrosive (Hazard Code C), or
both; or
2)
Listed as a hazardous waste in 35 Ill. Ada. Code
721.Subpart’D, solely because it is reactive
(Hazard Code R) for characteristics other than
The regulations in this Subpart apply to owners or
operators of facilities that incinerate hazardous waste
incinerators
(as defined in 35 Ill. Adm. Code 720.110),
except as 35 Ill. Ada. Code 724.101 provides otherwise.—
The following facility owners and operators are
considered to incinerate hazardous waste:
1)
Owners or operators of hazardous waste
incinerators
(as defined in 35 Ill. Ada. Code
720.110); and
2)
~
128—643
174
those listed in 35 Ill. Ada. Code 721.123,(a)(4)
and
(5), and will not be burned when other
hazardous wastes are present in the combustion
zone; or
3)
A hazardous waste solely because it possesses the
characteristic of ignitability, corrosivity, or
both,
as determined by the tests for
characteristics of hazardous wastes under 35 Ill.
Adm. Code 72l.Subpart C; or
4)
A
hazardous
waste
solely
because
it
possesses
the
reactivity characteristics described by
35
Ill.
Ada. Code 721.123
(a)(1),
(2),
(3),
(6),
(7) or
(8) and will not be burned when other hazardous
wastes are present in the combustion zone.
(Source:
Amended at 16 Ill. Reg.
,
effective
SUBPART
P:
THERMAL
TREATMENT
Section
725.470
Other
Thermal
Treatment
The
regulations
in
this
Subpart
apply
to
owners
and
operators
of
facilities
that
thermally
treat
hazardous
waste
in
devices
other
than
enclosed
devices
using
controlled
flame
combustion
except,
as
Section
725.101
provides otherwise.
Thermal treatment in
enclosed devices using controlled flame combustion is subject to
the requirements of Subpart 0 if the unit is an incinerator,
and
35
Ill.
Adm. Code 726.Subpart
H,
if the unit is a boiler or
industrial furnace as defined in 35
Ill. Ada. Code 720.110.
(Source:
Amended at
16 Ill. Reg.
,
effective
SUBPART AA:
AIR EMISSION STANDARDS FOR PROCESS VENTS
Section 725.935
Recordkeeping Requirement’s
a)
Compliance Required.
1)
Each owner or operator subject to the provisions
of this Subpart shall comply with the
recordkeeping requirements of this Section.
2)
An owner or operator of more than one hazardous
waste management unit subject to the provisions of
this Subpart may comply with the recordkeeping
requirements for these hazardous waste management
units
in one recordkeeping system if the system
identifies each record by each hazardous waste
128—644
175
management
unit.
b)
Owners
and
operators
shall record the following
information in the facility operating record:
1)
For facilities that comply with the provisions of
SectiOn 725
•
933(a) (2), an implementation schedule
that includes dates by which the closed-vent
system and control device will be installed and in
operation.
The schedule must also include a
rationale of why the installation cannot be
completed at an earlier date.
The implementation
schedule must be in the facility operating record
by the effective date that the facility becomes
subject to the provisions of this Subpart.
2)
Up-to-date documentation of compliance with the
process vent standards in Section 725.932,
including:
A)
Information and data identifying all affected
process vents’,
annual throughput and
operating hours of each affected unit,
estimated emission rates for each affected
vent and for the overall facility (i.e., the
total emissions for all affected vents at the
facility),
and the approximate location
within the facility of each affected unit
(e.g.,
identify the hazardous waste
management units on a facility plot plan).
B)
Information and data supporting determination
of vent emissions and emission reductions
achieved by add—on control devices based on
engineering calculations or source tests.
For the purpose of determining compliance,
determinations of vent emissions and emission
reductions must be made using operating
parameter values
(e.g.,
temperatures, flow
rates, or vent stream organic compounds and
concentrations)
that
represent
the
conditions
that result in maximum organic emissions,
such as when the waste management unit is
operating at the highest load or capacity
level reasonably expected to occur.
If the
owner or operator takes any action (e.g.,
managing a waste of different composition or
increasing operating hours of affected waste
management units)
that would result
in an
increase
in
total
organic
emissions
from
affected
process
vents
at
the
facility,
then
a
new
determination
is
required.
128—645
176
3)
Where
an owner or operator chooses to use test
date
to
determine
the
organic
removal
efficiency
or
total
organic
compound concentration achieved
by
the
control
device,
a
performance
test
plan.
The
test
plan
must
include:
A)
A
description
of
how it
is
determined
that
the
planned
test
is
going
to
be
conducted
when
the
hazardous
waste
management
unit
is
operating at the highest load or capacity
level reasonably expected to occur.
This
must include the estimated or design flow
rate and organic content of each vent stream
and define the acceptable operating ranges of
key process and control device parameters
during the test program.
B)
A detailed engineering description of the
closed—vent system and control device
including:
i)
Manufacturer’s name and model number of
control device.
ii)
Type of control device.
iii) Dimensions of the control device.
iv)
Capacity.
v)
Construction materials.
C)
A detailed description of sampling and
monitoring procedures,
including sampling and
monitoring locations in the system, the
equipment to be used, sampling and monitoring
frequency, and planned analytical procedures
for sample analysis.
4)
Documentation of compliance with Section 725.933
must include the following information:
A)
A list of all information references and’
sources used in preparing the documentation.
B)
Records~including the dates of each
compliance test required by Section
725.933(j).
C)
If engineering calculations are used,
a
design analysis, specifications,
drawings1
128—646
177
schematics, and piping and instrumentation
diagrams ‘based on the appropriate sections of
APTI
Course 415 (incorporated by reference in
35 Ill. Ada. Code 720.111) or other
engineering texts, approved by the Agency,
that present basic control device design
information.
Documentation provided by the
control device manufacturer or vendor that
describes the control device design in
accordance with subsections
(b) (4) (C) (i)
through
(vii)
may be used to comply with this
requirement.
The design analysis must
address the vent stream characteristics and
control device operation parameters as
specified below.
i)
For a thermal vapor incinerator, the
design analysis must consider the vent
stream composition, constituent
concentrations and flow rate.
The
design analysis must also establish the
design minimum and average temperature
in the combustion zone and the
combustion zone residence time.
ii)
For a catalytic vapor incinerator, the
design analysis must consider the vent
stream composition, constituent
concentrations, and flow rate.
The
design analysis must also establish the
design minimum and average temperatures
across the catalyst bed inlet and
outlet.
iii) For a boiler or process heater, the
design analysis must consider the vent
stream composition,
constituent
concentrations and flow rate.
The
.design analysis must also establish the
design minimum and average flame zone
temperatures, combustion zone residence
time and description of method and
location where the vent stream is
introduced into the Oombustion
zone.,
iv)
For a flare, the desIgn analysis must
consider the vent stream composition,
constituent ‘concentrations, and flow
rate.
The design analysis must also
consider the requirements specified in
Section 725.933(d).
128—647
178
v)
For a condenser, the design analysis
must consider the vent stream
composition, constituent concentrations,
flow rate, relative humidity and
temperature.
The design analysis must
also establish the design ,outlet organic
compound concentration level,
design
average temperature of the condenser
exhaust vent stream and design average
temperatures of
the
coolant fluid at the
condenser inlet and outlet.
vi)
For a carbon adsorption system such as a
fixed—bed adsorber that regenerates the
carbon bed directly onsite in the
control device, the design analysis must
consider the vent stream composition,
constituent concentrations,
flow rate,
relative humidity and temperature.
The
design analysis must also establish the
design exhaust vent stream organic
compound concentration level, number and
capacity of carbon beds,
type and
working capacity of activated carbon
used for carbon beds,
design total steam
flow over the period of each complete
carbon bed regeneration cycle, duration
of the carbon bed steaming and
cooling/drying cycles, design carbon bed
temperature after regeneration, design
carbon bed regeneration time and design
service life of carbon.
vii) For a carbon adsorption system such as a
carbon canister that does not regenerate
the carbon bed directly onsite in the
control device, the design analysis must
consider the vent stream composition,
constituent concentrations, flow rate,
relative humidity and temperature.
The
design analysis must also establish the
design outlet organic concentration
level,
capacity of carbon bed, type and
working capacity of activated carbon
used for carbon bed and design carbon
replacement interval based on the total,
carbon working capacity of the control
device and source operating schedule.
D)
A statement signed and dated by the owner or
operator certifying that the operating
parameters used in the design analysis
128—648
179
reasonably represent the conditions that
exist when the hazardous waste management
unit is or would be operating at the highest
load or capacity level reasonably expected to
occur.
E)
A statement signed and dated by the owner or
operator certifying that the control device
is designed to operate at an efficiency of 95
percent or greater unless the total organic
concentration limit of Section 725.932(a)
is
achieved at an efficiency less than 95 weight
percent or the total organic emission limits
of Section 725.932(a)
for affected process
vents at the facility are attained by a
control device involving vapor recovery at an
efficiency less than 95 weight percent.
A
statement provided by the control device
manufacturer or vendor certifying that the
control equipment meets the design
specifications may be used to comply with
this requirement.
F)
If performance tests are used to demonstrate
compliance,
all test results.
c)
Design documentation and monitoring operating and
inspection information for each closed—vent system and
control device required to comply with the provisions
of this Part must be recorded and kept up-to-date
in
the facility operating record.
The information must
include:
1)
Description and date of each modification that is
made to the closed—vent system or control device
design.
2)
Identification of operating parameter,
description
of monitoring device, and diagram of monitoring
sensor location or locations used to comply with
Section 725.933(f) (1) and
(2).
3)
Monitoring, operating and inspection information
required by Section 725
•
933 (f) ~through (k).
4)
Date, time and duration of each period that occurs
while the control device is operating when any
monitored parameter exceeds the value established
in the control device design analysis as specified
below:
A)
For a thermal vapor incinerator designed to
1,28—649
180
operate with a minimum residence time of 0.50
second at a minimum temperature of 760 C, any
period when the combustion temperature is
below. 760 C.
B)
For a thermal vapor incinerator designed to
operate with an organic emission reduction
efficiency of 95 percent or greater, any
period when the combustion zone temperature
is more than 28 C below the design average
combustion zone temperature established as a
requirement of subsection
(b) (4) (C)
(i).
C)
For a catalytic vapor incinerator, any period
when:
i)
Temperature of the vent stream at the
catalyst bed inlet is more than 28 C
below the average temperature of ‘the
inlet vent stream established as a
requirement of subsection
(b) (4) (C) (ii);
or
ii)
Temperature difference across the
catalyst bed is less than 80 percent of
the design average temperature
difference established as a requirement
of subsection
(b) (4) (C) (ii).
D)
For a boiler or process heater, any period
when:
i)
Flame zone temperature is more than 28 C
below the design average flame zone
temperature established as a requirement
of subsection
(b) (4) (C) (iii); or
ii)
Position changes where the vent stream
is introduced to the combustion zone
from the location ‘established as a
requirement of subsection
(b) (4) (C) (iii).
E)
For a flare, period when the pilot flame
is
not ignited.
F)
For a condenser that complies with Section
725.933(f) (2) (F) (i), any period when the
organic compound concentration level or
readings of organic compounds in the exhaust
vent stream from the condenser are more than
20 percent greater than the design outlet
organic compound concentration level
128—650
181
established as a requirement of subsection
(b) (4) (C)(v).
G)
For a condenser that complies with Section
‘725.933(f) (2) (F) (ii), any period when:
i)
Temperature of the exhaust, vent stream
from the condenser is more than
6 C
above the design average exhaust vent
stream temperature established as a
requirement of subsection
(b) (4) (C) (v).
ii)
Temperature of the coolant fluid exiting
the condenser is more than 6 C above the
design average coolant fluid temperature
at the condenser outlet established as a
requirement of subsection
(b) (4) (C) (v).
H)
For a carbon adsorption system such as a
fixed—bed carbon adsorber that regenerates
the carbon bed directly onsite in the control
device and complies with Section
725.933(f)(2)(G)(i), any period when the
organic compound concentration level or
readings of organic compounds in the exhaust
vent stream from the carbon bed are more than
20 percent greater than the design exhaust
vent stream organic compound concentration
level established as a requirement of
subsection
(b) (4) (C) (vi).’
I)
For a carbon adsorption system such as a
fixed—bed carbon adsorber that regenerates
the carbon bed directly onsite in the control
device and complies with Section
725.933(f) (2) (G) (ii), any period when the
vent stream continues to flow through the
control device beyond the predetermined
carbon’ bed regeneration time established as a
requirement of subsection
(b) (4) (C) (vi).
5)
Explanation for each period recorded under
subsection
(c) (4)
of the cause for control device
operating parameter exceeding the design value and
the measures implemented to correct the control
device operation.
6)
For carbon adsorption systems operated subject to
requirements specified in Section 725.933(g)
or
(h) (2), any date when existing carbon in the
control device is replaced with fresh carbon.
128—65 1
182
7)
For carbon adsorption systems operated subject to
requirements Specified in Section 725.933(h) (1), a
log that records:
A)
Date and time when control device is
monitored for carbon breakthrough and the
monitoring device reading.
B)
Date when existing carbon in the control
device
is
replaced
with
fresh
carbon.
8)
Date of each control device startup and shutdown.
d)
Records of the monitoring, operating and inspection
information required by subsections
(c) (3)
through
(8)
need be kept only
3 years.
e)
For a control device other than a thermal vapor
incinerator, catalytic vapor incinerator, flare,
boiler, process heater, condenser or carbon adsorption
system, monitoring and inspection information
indicating proper operation and maintenance of the
control device must be recorded in the facility
operating record.
f)
Up-to-date information and data used to determine
whether or not a process vent is subject to the
requirements in Section 725.932, including supporting
documentation as required by Section 725.934(d) (2),
when application of the knowledge of the nature ‘of the
hazardous wastestream or the process by which it was
produced is used, must be recorded in a log that is
kept in the facility operating record.
(Source:
Amended at
16 Ill. Reg.
,
effective
)
SUBPART BB:
AIR EMISSION STANDARDS FOR EQUIPMENT
LEAXS
Section 725.952
Standards: Pumps in Light Liquid Service
a)
Monitoring
1)
Each pump in light liquid service must be
monitored monthly to detect leaks by the methods
specified in Section 725.963(b),
except as
provided in subsections
(d),
(e) and
(f).
2)
Each pump in light liquid service must be checked
by visual inspection each calendar week for
indications of liquids dripping from the pump
seal.
128—652
183
b)
Leaks
1)
If an instrument reading of 10,000 ppm or greater
is measured, a’leak is detected.
2)
If there are indications of liquids dripping from
the pump seal,
a leak is detected.
c),
Repairs
1)
When a leak is detected,
it must be repaired as
soon as practicable, but not later than 15
calendar days after it is detected, except as
provided in Section 725.959.
2)
A first attempt at repair (e.g., tightening the
packing gland) must be made no later than 5
calendar days after each leak
is detected.
d)
Each pump equipped with a dual mechanical seal system
that includes a barrier fluid system is exempt from the
requirements of subsection
(a), provided the following
requirements are met:
1)
Each dual mechanical seal system must be:
A)
Operated with the barrier fluid at a pressure
that is at all times greater than the pump
stuffing box pressures; or
B)
Equipped with a barrier fluid degassing
reservoir that
is. connected by a closed—vent
system to a control device that complies with
the requirements of Section 725.960; or
C)
Equipped with a system that purges the
barrier fluid into a hazardous wastestream
with ~nodetectable emissions to the
atmosphere.
2)
The barrier fluid system must. not be a hazardous
waste with organic concentrations 10 percent or
greater by weight.
3)
Each barrier fluid system must be equipped with a
sensor that will detect failure of the seal
system, the barrier fluid system, or both.
4)
Each pump must be checked by visual inspection,
each calendar week,
for indications of liquids
dripping from the pump seals.’
128—653
184
5)
Alarms
A)
Each sensor as described in subsection
(d) (3)
must be checked daily or be equipped with an
audible alarm that must be checked monthly to
ensure that it is functioning properly.
B)
The owner or operator shall determine,
based
on design considerations and operating
experience,
a criterion that indicates
failure of the seal system, the barrier fluid
system, or both.
6)
Leaks
A)
If there are indications of liquids dripping
from the pump seal or the sensor indicates
failure of the seal system, the barrier fluid
system, or both based on the criterion
determined in subsection
(d) (5) (B),
a leak is
detected.
B)
When a leak is detected,
it must be repaired
as~soon as practicable, but not later than 15
calendar days after it is detected, except as
provided in Section 725.959.
C)
A first attempt at repair
(e.g., relapping
the seal) must be made no later than 5
calendar days after each leak is detected.
e)
Any pump that is designated,
as described in Section
725.964(g) (2), for no detectable emissions,
as
indicated by an instrument reading of less than 500 ppm
above background,
is exempt from the requirements of
subsections
(a),
(c) and
(d),
if the pump meets the
following requirements:
1)
Must have no externally actuated shaft penetrating
the pump housing.
2)
Must operate with no detectable emissions as
indicated by an instrument reading of less than
500 ppm above background as measured by the
methods specified in Section 725.963(c).
3)
Must be tested for compliance with subsection
(a)
(2
(e) (2)
initially upon designation, annually
and at other times as specified by the Agency
pursuant to Section 725.950(e).
128—654
185
f)
If any pump is equipped with a closed-vent system
capable of capturing and transporting any leakage from
the seal or seals to a control device that complies
with the requirements of Section 725.960,
it is exempt
from the requirements of subsections
(a) through (e).
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
128—655
186
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER I:
POLLUTION CONTROL BOARD
SUBCHAPTER
c:
HAZARDOUS
WASTE
OPERATING REQUIREMENTS
PART
726
STANDARDS
FOR THE
MANAGEMENT
OF SPECIFIC
HAZARDOUS
WASTE
AND
SPECIFIC TYPES OF
HAZARDOUS
WASTE
MANAGEMENT
FACILITIES
SUBPART
C:
RECYCLABLE
MATERIALS
USED
IN
A
MANNER
CONSTITUTING DISPOSAL
Section
726.120
Applicability
726.121
Standards applicable to generators and transporters of
materials used in a manner that constitutes disposal
726.122
Standards applicable to storers, who are not the
ultimate users, of materials that are to be used in a
manner that constitutes disposal
726.123
Standards applicable to users of materials that are
used in a manner that constitutes disposal
SUBPART D:
HAZARDOUS WASTE BURNED
FOR ENERGY RECOVERY
Section
726.130
Applicability (Repealed)
726.131
Prohibitions- (Repealed)
726.132
Standards applicable to generators of hazardous waste
fuel
(Repealed)
726.133
Standards
applicable
to
transporters
of
hazardous
waste
fuel
(Repealed)
726.134
Standards applicable to marketers of hazardous waste
fuel (Repealed)
726.135
Standards applicable to burners of hazardous waste fuel
(Repealed)
726.136
Conditional exemption for spent materials and by-
products exhibiting a characteristic of hazardous waste
(Repealed)
SUBPART E:
USED OIL BURNED FOR ENERGY RECOVERY
Section
726.140
Applicability
726.141
Prohibitions
726.142
Standards applicable to generators of used oil burned
for energy recovery
726.143
Standards applicable to marketers of used oil burned
for energy recovery
726.144
Standards applicable to burners of used oil burned for
energy recovery
128—656
187
SUBPART
F:
RECYCLABLE MATERIALS UTILIZED FOR PRECIOUS METAL
RECOVERY
Section
726.170
Section
726.180
Applicability and requirements
SUBPART G:
SPENT LEAD-ACID BATTERIES BEING RECLAIMED
Applicability and requirements
SUBPART H:
HAZARDOUS
WASTE BURNED
IN
BOILERS
AND
INDUSTRIAL FURNACES
Applicability
Management prior to Burning
Permit standards for Burners
Interim status standards for Burners
Standards to control Organic Emissions
Standards to control PM
Standards to control Metals Emissions
Standards to control HC1 and Chlorine Gas Emissions
Small quantity On-site Burner Exemption
Low risk waste Exemption
Waiver of DRE trial burn for Boilers
Standards for direct Transfer
Regulation of ‘Residues
Extensions of Time
Appendix A
Appendix B
Appendix C
Appendix D
Appendix E
Appendix F
Appendix G
Appendix H
Appendix
I
Appendix J
Appendix K
Appendix L
Table A
Tier
I and Tier II Feed Rate and Emissions
Screening Limits for Metals
Tier
I Feed Rate Screening Limits for Total
Chlorine and Chloride
Tier II Emission Rate Screening Limits for Free
Chlorine and Hydrogen Chloride
Reference Air Concentrations
Risk Specific Doses
Stack Plume Rise
Health-Based Limits for Exclusion of Waste-Derived
Residues
Potential. PICs for Determination of Exclusion of
Waste-Derived Residues
Methods Manual for Compliance with BIF Regulations
Guideline on Air quality Models
Lead-Bearing Materials That May be Processed in
Exempt Lead Smelters
Nickel or Chromium—Bearing Materials that may be
Processed in Exempt Nickel—Chromium Recovery
Furnaces
Exempt Quantities for Small Quantity Burner
Exemption
Section
726.200
726.201
726.202
726.203
726.
204
726.205
726.206
726.207
726.208
726.209
726.
210
726.211
726.212
726.219
128—657
188
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
111½, pars.
1022.4 and 1027).
SOURCE:
Adopted
in R85—22 at 10 Ill. Reg.
1162, effective
January 2, 1986; amended in R86—1 at 10 Ill.
Reg. 14156,
effective August 12,
1986; amended in R87—26 at 12
Ill. Reg.
2900, effective January 15,
1988; amended in R89—l at 13 Ill.
Reg.
18606,
effective November 13, 1989;
amended in R90-2 at 14
Ill. Reg.
14533, effective August 22,
1990; amended in R90-i1 at
15 Ill. Reg. 9727, effective June 17,
1991;
amended in R91—13 at
16 Ill. Reg.
,
effective
SUBPART D:
HAZARDOUS
WASTE BURNED FOR ENERGY RECOVERY
Section
726.130
Applicability
(Repealed~
a)
The regulations of this Subpart apply to hazardous
wa~~e~
Lnu’~ui-c DUi-I1~Uior
energy recovcry in any
boiler or industrial furnace that is not regulated
.
—
35 Ill.Adm. Code 724 or 725.Subpart 0 except
provided by 3ubsection
(b).
Such hazardous wastes
burned for energy recovery are termed “hazardous waste
fuel”.
Fuel produced from hazardous waste processing,
by blending or other treatment is also hazzirdou~wastc
fuel.
(The regulations do not.apply, however,
to gas
recovered from hazardous waste management activities
when such ~
is burned for enerrn~recovery).
b)
The following ~
wastes arc not regulated under
thi3 Subpart:
1)
Used oil -burncd for energy recovery that is also a
hazardous waste solely because it exhibits a
characteristic of hazardous waste identified in 35
Ill.Adm. Code 721.Cubpart C.
Such used oil is
subject to rcgulation undcr Subpart E rather than
this
Subpart;
and
2)
Hazardous
wastes
that
are
exemmt
f’ir~m
i1~i~r~n
under the provisions of
35
Ill.Athn. Code 721.104
and 721. 106(a) (3) (E) through
(I)
and hazardous
wastes that are subject to the special
requirements for small quantity generators under
the nrovisions of 35 Ill.Adm. Code 721.105.
(Source:
Repealed at 16
Ill. Reg.
,
effective
)
Section 726.131
Prohibitions
(Repealed)
:c
naza
128—658
189
1)
To persons
who’
have notified UCEPA of their
flazar~ou3
~
identification
.~i.
number
gnu
(35 Ill.Adm.
nave
Code
a
UCEPA
722.112);
a~4
2)
If
the fuel is
burned,
to persons who burn the
fuel in
boilers
or
industrial
furnaces
identified
il_I SUDSCCt1Ofl
(n).
b)
HaEardous waste fuel may be
burned
for energy recovery
in only the following devices:
Inaustriai rurnaccs identifled in 35 iii.Aam. Coa
720.110;
noiler, as defined in 35 Ill.Adm. Code 720.110
tnut arc iaen’ciriea as roijows:
A)
Industrial boilers located on the site of a
facility engaged in a manufacturing process
where substanccs arc transformed into new
products,
including the component parts of
Droducts, by mechanical or chemical
nrocesses
-
U)
utiiity DoilerS
U3CU
tO t~1~OaUCC
eicotr.C
powcr,
steam
‘~‘
h~i~
or cooled air or other
gases or fluids for 3015.
r~i
r1u
ruei. wnicn
contains
any nu~araouswa~t~
Tht~V
~urnca in any cement kiln which is locatea witnin tne
boundaries of any incorporated municipality with a
population greater than 500,000
(based on the most
recent census statistics) unless such kiln fully
compiic~witn reguiations unacr 35
iii..i~o.m.
Code 702,
703,
724 and 725 that are applicable in incinerators.
(Source:
Repealed at 16 -Ill. Reg.
,
effective
Section 726.132
Standards applicable to generators of hazardous
waste fuel (Repealed)
a)
Generators of hazardous waste that is used as
a fuel or
used to produce a fuel are subject to 35 Ill.Adm Code
~?.
,
b)
Generators who market hazardous waste fuel to a burner
also
are subject to Section 726.134
128—659
190
c)
Generators who are burners also are subject to &ec~
726.
135-~-
(Source:
Repealed
at
16
Ill.
Reg.
)
effective
Section 726.133
Standards applicable to transporters of
hazardous waste fuel
(Repealed).
Transporters
of
used to produce
hazardous waste fuel
a fuel)
arc subject
(and
to the
hazardous waste th~
~5 Ill.Adm.
Code
‘~
(Source:
Repealed at 16 Ill. Reg.
)
,
effective
Section 726.134
Standards applicable to marketers of hazardc
waste
fuel
(Repealed)
ni~ri
Ii~
—.
who di4~......
but
~.
waste fuel.
-~
n,,__~_S1_SS_1
1,,
1
,~,,
1
a_.,,,
n__S~
b)
Motification.
Notification of hazardous waste fuel
activities.
Even if a
marketer has previously noti:
UCEPA
of
the
marketer’s
hazardous
waste
management
activities and obtained a
-UCEPA
-identification
numbi
the marketer shall renotify t-~identify the marketei
hazardous- waste fuel activities.
C)
Storage.
The-applicable provisions of 35 Ill.Adm. (
702,
703,
722.1)4, 724.Cubparts A through L and
725.Cubparts A through L
—I
-~——-—~-
“1~-.
-tandards for generators In
_
marketer initiates a shipmE
—
ISA
_,s___
,s_t,
—
e~
_,.,_.s_
,‘L
I
quired notices.
marketcr,
the
shall obtain a one time
~4
~.L’~I
~
1I~
S.~w
5
£.
~W
~1w
~
~4,S.
~
ertifying that:
128—660
Persons who market hazardous waste fuel are called’ “~arkcte,rs
and are subject to the following requirements.
Marketers fl~c
generators who market hazardous waste fuel directly to a burn
persons who receive hazardous ‘waste from generators
and
produ
process or blend -hazardous waste fuel from these hazardous wa
~
process or blend
hazard
d)
—
..
.a..
a.2ww.
a a.w
Ill.Adm.
Code
722
-thefl
_
r~f
hn~rinii~
i~t~
f~I
—
191
A)
Theeburner or marketer
identified the burner
has notified
or marketer’s
UCEPA and
waste-as-
fuel activities; and
B)
If the recipient~i~
hiarni~i
f~h~
hi
wn~r
burn tnc nazaraogs waste fuel only in an
industrial furnace or boiler identified in 35
Ill.Adm.
Code
726.131(b).
mn~~i~
~r*ri
+h~
firrt
shipment of
-~•
-.
-—
recordkeeping requirements of 35
Ill.Adin. Code 722,
724
and 725,
a marketer shall keep a copy of each
certification notice the marketer receives or sends for
three
years
from the date the marketer last engages in
a hazardous waste fuel marketing transaction with the
person who sends or receives the certification notice.
(Source:
Repealed
at
16
Ill.
Reg.
,
effective
Section 726.135
Standards applicable to burners or hazardous
waste fuel
(Repealed)
Owners and operators of industrial furnaces and boilers
identified in Section 726.131
(b) that burn hazardous waste fuel
-ir~
~
ini
~iri~~*nhini~t~ tci thp
fc~1
1riuinr~
rnii-rms~nti~
———
J
a)
Prohibitions.
The prohibitions under section
726.131(b)
—I
activities.
Even
if a burner has previously notified
USEPA of the burner’s hazardous waste management
activities and obtained a UCEPA identification number,
t~hs~hiii-rtt-i-
~hn11 renotify to ideri$-if.r ~
h~ii-~i-’~
fuel activities.
1-)
ror short term
their hazardou:
128—661
umulatic
_S_
,~~__1
by generators who burn
n -site, the applicable
/
hazardous waste fuel from anotner
—-
—‘~—
-
marjcter shall provide the otner marJceter with a
one time written and signed certification that the
marketer has notified UCEPA under Section 3010 of
the flesource Conservation and flecovery Act and
identified the marketer’s hazardous waste fuel
~a,_.___
V
~
,
and
192
2)
For existing storage facilities, the applicable
provisions of 35 I1l.Adm. Code 702, 703 and
725.CuDparcs A througn ~
ana
3)
For new storage facilities,
the
applicable
provisions of 35 Ill.Adm. Code 702,
703 and
through L
d)
flequired notices.
Before a
shipment of hazardous waste
burner
fuel fr
accepts the first
om marketer, the
burner shall provide the marketer a one time written
4
r,i-~i~
rir~i
4
r~
r~~1-+
i
fyi
rtrr
P~hnP
t
—_-,..——
1)
The burner has notified UCEPA arid identified the
bin—n~r’~
tz~~itr~
a~—fu~1
n~tiv4ti~~
nnd
the fuel
w.~J
i-..
boiL....
rurnace identified in
Section 726.131(b).
~uKecping.
in aaai’cion to, the applicable
recordiceeping requirements of 35 Ill.Adm. Code 724
and
725 a burner shall keep a copy of each certification
notice that the burner sends to a marketer
fort three
years from the date the burner last receives hazardous
waste fuel from that marketer.
(Source:
Repealed at 16 Ill.
Reg.
,
effective
)
SUBPART E:
USED OIL BURNED FOR ENERGY RECOVERY
Section 726.140
Applicability
a)
The regulations of this Subpart apply to used oil that
is burned for energy recovery in any boiler or
industrial furnace that is not regulated under 35
Ill.
Adm.
Code 724.
or 725.Subpart 0, except as provided by
subsection
(c) and
(e).
Such used oil is termed “used
oil fuel”.
Used oil fuel includes any fuel produced
from used oil by processing,
blending or other
treatment.
b)
“Used oil” means any oil that has been refined from
crude oil, used and, as a result of such use,
is
contaminated by physical or chemical impurities.
c)
Except as provided by subsection
(d), used oil that is
mixed with hazardous waste and burned for energy
recovery is subject to regulation as hazardous waste
fuel under Subpart DII.
Used oil containing more than
1000 ppm of total halogens is presumed to be a
hazardous waste because it has been mixed with
Y~1
1
rn
-~
--
p.
—
~.
rn
~)
The
hiiivi,~
128—662
193
halogenated hazardous waste listed in 35 Ill. Adm. Code
721.Subpart D.
Persons may rebut this presumption by
demonstrating that the used oil does not contain
hazardous waste
(for example, by showing that the used
oil does not contain significant concentrations of
halogenated hazardous constituents listed in 35 Ill.
Adju.
Code ‘721.Subpart H).
d)
Used oil burned for energy recovery is subject to
regulation under this Subpart rather than as hazardous
waste fuel under Subpart Dfl if it is a hazardous waste
solely because it:
1)
Exhibits a characteristic of hazardous waste
identified in 35 Ill. Adm. Code 72l.Subpart C,
provided that it is not mixed with a hazardous
waste; or
2)
Contains hazardous waste generated only by a
person subject to the special requirements for
small
quantity
generators
under
35
Ill.
Adm.
Code
721.105.
e)
Except as provided by subsection
(c), used oil burned
for energy.recovery,
and any fuel produced from used
oil by processing, blending or other treatment,
is
subject to regulation under this Subpart unless it is
shown not to exceed any of the allowable level of the
constituents and properties in the specification shown
in the following table.
Used oil.fuel that meets the
specification is subject only to the analysis and
recordkeeping requirements under Section 726.143(b) (1)
and
(b)
(6).
Used oil fuel that exceeds any
specification level is termed “off—specification used
oil
fuel”.
USED OIL EXCEEDING
ANY
SPECIFICATION
LEVEL
IS SUBJECT TO THIS SUBPART WHEN
BURNED FOR ENERGY RECOVERY
Constituent/Property
Allowable Level
Arsenic
5 ppm max
Cadmium
2 ppm max
Chromium
10 ppm max
Lead
100 ppm max
Flash
Point
100
degree
F
mm
Total Halogens
4000 ppm max
1)
The specification does not apply to used oil or
fuel mixed with a hazardous waste other than small
quantity generated hazardous waste.
128—663
194
2)
Used oil containing more than 1000 ppm total
halogens
is
presumed
to
be
a
hazardous
waste
under
the rebuttable presumption provided under
subsection
(c).
Such used oil is subject to
Subpart D rather than this Subpart when burned for
energy recovery unless the presumption of mixing
can be successfully rebutted.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
SUBPART H:
HAZARDOUS WASTE BURNED IN BOILERS
AND
INDUSTRIAL FURNACES
Section
726.200
Applicability
~j
The regulations of this Subpart apply to hazardous
waste burned or processed in a boiler or industrial
furnace
(BIF)
(as defined in 35 Ill.
Adm. Code 720.110)
irrespective of the purpose of burning or processing,
except
as
provided
by
subsections
(b),
(c),
(dL
and
(f).
In this Subpart, the term “burn” means burning
for
energy
recovery or destruction, or processing for
materials-
recovery
or
as
an
ingredient.
The
emissions
standards of Sections 726.204. 726.205,
726.206 and
726.207 apply to facilities operating under interim
status or under a
RCRA
permit as specified in Sections
726.202 and 726.203.
BOARD NOTE:
This provision does not apply to coke
ovens processing coke by—products wastes exhibiting the
toxicity
characteristic
identified
in
35
Ill.
Adm.
Code
721.124
pending
completion
of
a
rulemaking
proposed
by
USEPA on July 26,
1991
(56 Fed. Reg. 35787).
When that
rulemaking is complete, this note will be removed.
~j
The following hazardous wastes and facilities are not
subject
to
regulation
under
this
Subpart:
fl
Used oil burned for energy recovery that is also a
hazardous waste solely because it exhibits
a
characteristic of hazardous waste identified in 35
Ill. Adm. Code 721.Subpart
~.
Such used oil
is
subiect to regulation under Subpart E rather than
this
Subpart
~J..
Gas recovered from hazardous or solid waste
landfills when such gas is burned for energy
recovery
128—664
195
fl
Hazardous wastes that are exempt from regulation
under 35 Ill.
‘Adin.
Code 721.104 and
721.106(a)13)’(E)
—
(H). and hazardous wastes that
are subiect to the special requirements for
conditionally exempt small auantity generators
under 35 Ill.
Adm. Code
721.105;
and
.4j
Coke ovens,
if the only hazardous waste burned is
USEPA Hazardous Waste No.
K087, decanter
tank
tar
sludge from coking operations.
~j
Owners and operators of smelting. melting and refining
furnaces
(including
pyronietallurczical
devices
such
as
cu~olas.sjntering machines. roasters and foundry
furnaces, but not including cement kilns, aggregate
kilns or halogen acid furnaces burning hazardous waste)
that process hazardous waste solely for metal recovery
are conditionally exempt from regulation under this
Subpart, except for Sections 726.201 and 726.212.
fl.
To
be
exempt
from
Sections
726.202
through
726.211, an owner or operator of a metal recovery
furnace shall comply with the following
reci-uirements.
except that an owner or operator of
a lead or a nickel—chromium recovery furnace, or a
metal recovery furnace that burns ba~housebags
used to capture metallic dust emitted by steel
manufacturing, shall comply with the requirements
of
subsection
(c)(3):
~J.
Provide a one-time written notice to the
Agency indicating the following:
j)
The owner or operator claims exemption
under this subsection
iiL
The hazardous waste is burned solely for
metal recovery consistent with the
provisions of subsection
(c) (2):
iii) The hazardous waste contains recoverable
levels of metals;
and
.jyj
The owner or operator will comply with
the sampling and analysis and
recordkeeping requirements of this
subsection
~j
Sample and analyze the hazardous waste and
other feedstocks as necessary to com~lvwith
the requirements of this subsection under
procedures specified by ‘Test Methods for
128—665
196
Evaluating Solid Waste. Physical/Chemical
Methods, SW—846. incorporated by reference in
35 Ill.
Adm. Code 720.111 or alternative
methods that meet or exceed the SW-846 method
performance capabilities.
If SW-846 does not
prescribe a method for a particular
determination, the owner or operator shall
use the best available method:
and
çj
Maintain at the facility for at least three
years records to document compliance with the
provisions of this subsection including
limits on levels of toxic organic
constituents and Btu value of the waste,
and
levels of recoverable metals in the hazardous
waste compared to normal nonhazardous waste
feedstocks.
21
A
hazardous waste meeting either of the following
criteria is not processed solely for metal
recovery:
~j
The hazardous waste has a totalconcentration
of
organic compounds listed in 35 Ill.
Adm.
Code
721.Appendix
H.
exceeding
500
ppm
by
weight, as fired,
and so is considered to be
burned for destruction.
The concentration of
organic compounds in a waste as—generated may
be reduced to the 500
ppm
limit
by
bona
fide
treatment that removes or destroys organic
constituents.
Blending for dilution to
meet
the 500 ppm limit is prohibited and
documentation that the waste has not been
impermissibly diluted must be retained in the
records required by subsection
(C)
(1) (C);
or
~j
The hazardous waste has a heating value of
5,000_Btu/lb or more,
as—fired, and is
so
considered to be burned as fuel.
The heating
value of a waste as—generated may be reduced
to
below
the 5.000 Btu/lb limit by bona fide
treatment that removes or destroys organic
constituents.
Blending for dilution to meet
the 5.000 Btu/lb limit isprohibited and
documentation that the waste has not been
impermissibly diluted must be retained in the
records required by subsection
(C)
(1) (C).
fi
To
be
exempt
from
Sections
726.202
—
726.211, an
owner
or
operator
of
a
lead
or
nickel—chromium
recovery
furnace,
or
a
metal
recovery furnace that
burns
a
baghouse
gas
used
to
capture
metallic
128—66 6
197
dusts emitted by steel manufacturing must provide
a one-time written notice to the Agency
identifying each hazardous waste burned and
specifying whether the owner or operator claims an
exemption for each waste under this subsection or
subsection
(c) (1).
The owner
or operator shall
comply with the requirements of subsection
(c) (1)
for those wastes claimed to be exempt under that
subsection and shall com~lvwith the requirements
below for those wastes claimed to be exempt under
this subsection.
~j
The hazardous wastes listed
in
Appendices
K
and L and baghouse baas used to capture
metallic
dusts
emitted
by
steel
manufacturing
are exempt from the requirements of
subsection
Cc) (1). provided that:
jj
A waste listed in Appendix K must
contain recoverable levels of lead.
A
waste listed in Appendix L must contain
recoverable levels of nickel or chromium
and baghouse ba~sused to capture
metallic
dusts
emitted
by
steel
manufacturing must contain recoverable
levels of metal; and
jjj
The waste does not exhibit the Toxicity
Characteristic of 35
Ill.
Adm. Code
721.124 for an organic constituent; and
iii) The waste is not a hazardous waste
listed
in 35 Ill. Adm. Code 721.Subpart
D because
it is listed for an organic
constituent as identified in 35 Ill.
Adm. Code 721.Appendix G; and
i~1
The owner or operator certifies in the
one—time notice that hazardous waste is
burned under the provisions of
subsection
(c) (3) and that sampling and
analysis will be conducted or’ other
information will be obtained as
necessary to ensure continued compliance
with these requirements.
Sampling and
analysis must be conducted according to
subsection
(C) (1) (B) and records to
document compliance with Subsection
Lc) (3) must be kept for at least three
years.
128—667
198
~
The Agency may decide on a case—by—case basis
that
the
toxic
organic
constituents
in
a
material
listed
in
Appendix
K
or
L
that
contains a total concentration of more than
500 ppm toxic organic compounds listed in 35
Ill. Adm. Code 721.Apperidix H may pose a
hazard to
human
health and the environment
when burned in a metal recovery furnace
exempt from the requirements of this Subpart.
In_that situation,
after adequate notice and
opportunity for comment, the metal recovery
furnace_will become subject to the
requirements of this Subpart when burning
that material.
In making the hazard
determination, the Agency shall consider the
following
factors:
j).
The concentration and toxicity of
organic constituents in the material
and
jJJ.
The level of destruction of toxic
organic constituents provided by the
furnace:
and
iii) Whether the acceptable ambient levels
established
in
Appendices
D
or
E
will
be
exceeded for any toxic organic compound
that may be emitted based on dispersion
modeling
to predict the maximum annual
average off—site ground level
concentration.
~j
The standards for direct transfer operations under
Section 726.211 apply only to facilities sub-lect to the
permit standards of Section 726.202 or the interim
status
standards
of
Section
726.203.
~
The management -standards for residues under Section
726.212 apply to any BIF burning hazardous
waste.
il
Owners and operators of smelting. melting and refining
furnaces
(including pyrometallurgical devices such as
cupolas. sintering machines. roasters and foundry
furnaces)
that process hazardous waste for recovery of
economically significant amounts of the precious metals
gold, silver, platinum,
palladium, iridium, osmium,
rhodium
or
ruthenium,
or
any
combination
of
these,
are
conditionally exempt from regulation under this Subpart
except for Section 726.212.
To be exempt from Sections
726.202
-
726.211 an owner or operator shall:
128—668
199
jj
Provide a one-time written notice to the Agency
indicating the following:
~j
The owner or operator claims exemption under
this section
~j.
The
hazardous
waste
is
burned
for
legitimate
recovery
of
~reci~ous
metal;
and
ci
The owner or operator will com~lvwith the
samnling and analysis and recordkeeping
reauirements
of
this
section
fi
Sample and analyze the hazardous waste as
necessary to document that the waste is burned for
recovery of economically significant amounts of
precious metal using procedures specified by Test
Methods for Evaluating Solid Waste.
Physical/Chemical Methods, SW-846, incorporated by
reference in 35 Ill. Adm. Code 720.111 or
alternative methods that meet or exceed the SW—846
method performance capabilities.
If SW-846 does
not
prescribe
a
method
for
a
particular
determination, the owner or operator shall use the
best
available
method:
and
fi
Maintain at the facility
for
at
least
three
years
records to document that all hazardous wastes
burned are burned for recovery
of
economically
significant amounts of precious metal.
gJ
Abbreviations and definitions.
The following
definitions and abbreviations are used in this Subpart:
“APCS” means air pollution control system.
“BIF” means boiler or industrial furnace.
“Carcinogenic metals” means arsenic, beryllium,
cadmium and chromium.
“CC”
means carbon monoxide.
“Continuous monitor”
is a monitor which
continuously samples the re~latedparameter
without interruption, and evaluates the detector
response at least once each 15 seconds, and
computes and records the average value at least
every 60 seconds.
“DRE” means destruction or removal efficiency.
128—669
200
“cu m” means cubic meters.
“E”
means
“ten
to
the”.
For
example,
“XE—Y”
means
“X times ten to the —Y power”.
“Feed rates” are measured as specified in Section
726.202(e) (6)
“Good engineering practice stack height” is as
defined by 40 CFR 51.100(u).
incorporated by
reference in 35 Ill. Adm. Code 720.111.
“HC” means hydrocarbon.
“HCl” means hydrogen chloride gas.
“Hourly rolling average” means the arithmetic mean
of the 60 most recent 1—minute average values
recorded
by the continuous monitoring system.
“K” means Kelvin.
“kVA” means kilovolt amperes.
“MEl”- means maxi’mum exposed individual.
“MEl location” means the point with the
ma~m11m
annual average off—site
(unless on—site is
required) ground level concentration.
“Noncarcinogenic metals” means antimony, barium,
lead, mercury, thallium and silver.
“One hour block average” means the arithmetic mean
of the one minute averages recorded during the 60—
minute period beginning at one minute after the
beginning of preceding clock hour
“PlC” means product of incomplete combustion.
“PM”
means
particulate
matter.
“POHC” means principal organic hazardous
constituent.
“ppmv” means parts per million by volume.
“OA/OC” means quality assurance and quality
control.
128—670
201
“Rolling averaae for the selected averaging
period” means the arithmetic mean of one hour
block averages for the averaging period.
“RAC” means reference air concentration,
the
acceptable ambient level for the noncarcinogenic
metals for purposes of this Subpart.
RAC5 are
specified in Appendix D.
“RSD” means risk—specific dose, the accentable
ambient level for the carcinogenic metals for
purposes of this Subpart.
RSDs are specified in
Appendix E.
“SSU” is
a unit of viscosity.
“TCLP test” means the toxicity characteristic
leaching Procedure of 35 Ill.
Adm. Code 721.124.
“Tier I”.
See Section 726.206(b).
.
See Section 726.206(c).
“Tier III”.
See Section 726.206(d).
“TESH” means terrain—adjusted effective stack
height
(in meters).
“Toxicity equivalence”
is estimated, Pursuant to
Section 726.204(e). using “Procedures for
Estimating the Toxicity Equivalence of Chlorinated
Dibenzo—p—Dioxin and Dibenzofuran Congeners”
in
Appendix I
(“eye”).
“ug” means microgram.
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section 726.201
Management prior to Burning
~j
Generators.
Generators of hazardous waste that is
burned in a BIF are subiect to 35 Ill. Adm. Code 722.
~
Transporters.
Transporters of hazardous waste that is
burned in a BIF are subject to 35 Ill. Adm. Code 723.
gj
Storage
facilities.
fl
Owners and operators of facilities that store
hazardous waste that is burned in a BIF are
subiect to the applicable provisions of 35 Ill.
128—671
202
Adm. Code 724.Subparts A through L.
35
Ill.
Adin.
Code 725.Subparts A through L and 35 Ill. Adm.
Code 702 and 703, except as provided by subsection
(c)(2).
These standards a~~lv
to storage by the
burner as well as to storage facilities operated
by intermediaries (processors, blenders,
distributors.
etc.)
between
the
generator
and
the
burner.
21
Owners and operators of facilities that burn,
in
an on-site BIF exempt from regulation under the
small auantity burner provisions of Section
726.208. hazardous waste that they generate are
exempt from regulation under 35 Ill.
Adin. Code
724.Subparts A through L.
35
Ill. Adm. Code
725.Subparts A through L and 35 Ill. Adm. Code 702
and 703 with respect to the storage of mixtures of
hazardous waste and the primary fuel to the BIF in
tanks that feed the fuel mixture directly to the
burner.
Storage of hazardous waste prior to
mixing with the primary fuel is sub-lect to
regulation as prescribed in subsection
(c) (1).
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section 726.202
Permit standards for Burners
~j
Applicability.
jj
General.
Owners and operators of BIFs burning
hazardous waste and not operating under interim
status
shall
comply with the requirements of this
Section and 35 Ill. Adm. Code 703.208 and 703.232.
unless exempt under the small quantity burner
exemption of Section 726.208.
21
A~~licability
of 35 Ill.
Adm.
Code 724 standards.
Owners_.and operators of BIFs that burn hazardous
waste are subject to the following provisions of
35
Ill. Adm. Code 724. except as provided
otherwise by this Subpart:
~j
In
Subpart A
(General).
724.104
~
In Subpart B (General facility standards).
35
Ill.
Adm.
Code
724.111
—
724.118:
~
In Subpart C (Preparedness and prevention),.
35
Ill. Adm. Code 724.131
—
724.137
128—672
203
Qj
In Subpart D (Contingency plan and emergen
procedures).
35
Ill. Adm. Code 724.151
-
724.156
&
In Subpart E
(Manifest system, recordkeeping
and reporting), the applicable provisions of
35 Ill.
Adm. Code 724.171
—
724.177
fi
In Subpart F
(Corrective Action),
35
Ill.
Adm.
Code 724.190 and 724.201
QI
In Subpart G (Closure and post-closure).
35
Ill. Adm. Code 724.211
—
724.215
~j
In Subpart H (Financial requirements),
35
Ill.
Adm. Code 724.241, 724.242.
724.243 and
724.247
-
724.251,
except that the State of
Illinois and the Federal government are
exempt from the requirements of
35’ Ill.
Adm.
Code 724.Subpart H;
and
fl
Subpart
BB
(Air emission standards for
equipment leaks), except 35 Ill.
Adlu.
Code
724.950(a).
kj
Hazardous waste analysis.
fl.
The owner or operator shall provide an analysis of
the hazardous waste that quantifies the
concentration of any constituent identified in 35
Ill. Adm. Code 721.Appendix H that is reasonably
be expected to be in the waste.
Such constituents
must be identified and quantified if present, at
levels detectable by analytical procedures
prescribed by Test Methods for Evaluating Solid
Waste.
Physical/Chemical Methods
(incorporated by
reference, see 35
Ill. Adm. Code 720.111).
Alternative methods that meet or exceed the method
performance capabilities of SW—846 methods may be
used.
If SW—846 does not prescribe a method for a
particular determination, the owner or operator
shall use the best available method. ‘The 35
Ill.
Adm. Code 721.Appendix H constituents excluded
from this analysis must be identified and the
basis for their exclusion explained.
‘
This
analysis must provide all information required by
this Subpart and 35 Ill. Adm. Code 703.208 and
703.232 and must enable the Agency to prescribe
such permit conditions as necessary to protect
human health and the environment.
Such analysis
must be included as a portion of the Part Bpermi~
application,
or.
for facilities operating under
128—673
204
the interim status standards of this Subpart,
as a
portion of the trial burn ~1an that may be
submitted before the Part B p~plicationunder
provisions of
35 Ill.
Adm.
Code 703.232(g) as well
as any other analysis required by the Agency.
Owners
and operators of BIFS not operating under
the interim status standards shall provide the
information required by 35 Ill.
Adm. Code 703.208
and 703.232 in the Part B a~p1icationto the
~reatest extent possible.
21
Throughout normal operation,
the owner or operator
shall conduct sampling and analysis as necessary
to ensure that the hazardous waste,
other fuels
and industrial furnace feedstocks fired into the
BIF are within the physical and chemical
composition
limits
specified
in the permit.
Emissions standards.
Owners and operators shall comply~
with emissions standards provided by Sections 726.204
through 726.207.
.~j
Permits.
fl
The- owner or operator shall burn only hazardous
wastes specified in the facility permit and only
under the operating conditions specified under
subsection
(e). except in a~~roved
trial burns
under the conditions specified in 35
Ill. Adm.
Code 703.232.
21
Hazardous wastes not specified in the permit must
not be burned until operating conditions have been
specified under a new permit or permi~,
modification, as applicable.
Operati~g
requirements
for new wastes must be based on
either trial burn results or alternative data
included with Part B of a permit application under
35 Ill.
Adm. Code 703.208.
fi
BIFs operating under the interim status standards
of Section 726.203 are permitted under procedures
provided by 35 Ill. Adm. Code 703.232(g).
A permit for a new BIF (those BIFs not operating
under the interim status standards) must establish
appropriate conditions for each of the applicable
requirements of this Section, including but not
limited to allowable hazardous waste firing rates
and operating conditions necessary to meet the
requirements of subsection
(e).
in order to com~lv
with the following standards:
128—674
205
~j
For the period beginning with initial
introduction of hazardous waste and ending
with initiation of the trial burn.
and only
for the minimum time required to bring the
device to a point of operational readiness to
cànduct a trial burn, not to exceed a
duration of 720 hours operating time when
burning hazardous waste., the operating
reauirements
must
be
those
most
likely
to
ensure compliance with the emission standards
of Sections 726.204 through 726.207. based on
the_Agency’s engineering judgment.
If the
applicant is seeking a waiver from a trial
burn to demonstrate conformance with a
particular emission standard, the operating
requirements during this initial periOd of
operation must include those specified by the
applicable provisions of Section 726.204,
Section 726.205. Section 726.206or Section
726.207.
The Agency shall extend the
duration of this period for up to 720
additional hours when good cause for the
extension is demonstrated by the applicant.
~j
For the duration of the trial burn,
the
operating requirements must be sufficient to
demonstrate compliance with the emissions
standards of Sections 726.204 through 726.207
and must be in accordance with the approved
trial
burn
plan
~
For the period immediately following
completion of the trial burn. and only for
the minimum period sufficient to allow sample
analysis. data computation, submission of the
trial burn results by the applicant, review
of the trial burn results and modification of
the facility permit by the Agency to reflect
the trial burn results, the operating
reauirements must be those most likely to
ensure compliance with the emission standards
Sections 726.204 through 726.207 based on the
Agency’s engineering iudcnnent.
~j
For the remaining duration of the permit. the
operating requirements must be those
demonstrated in
a trial burn or by
alternative data specified in 35 Ill.
Adm.
Code 703~208,as sufficient to ensure
compliance with the emissions standards of
Sections 726.204 through 726.207.
128—675
206
~j
Operating requirements.
~j.
General.
A BIF burning hazardous waste must be
operated in accordance with the operating
requirements specified in the permit at all times
when there is hazardous waste in the unit.
21
Requirements to ensure compliance with the organic
emissions standards.
~j
DRE (destruction or removal efficiency)
standard.
Operating conditions must be
specified either:
on a case—by—case basis
for each hazardous waste burned as those
demonstrated
(in a trial burn or by
alternative
data
as specified in 35 Ill.
Adin.
Code
703.208)
to
be
sufficient
to
com~1vwith
the DRE performance standard of Section
726.204(a);
or-.
as those special operating
requirements
provided
bY
Section
726.204(a) (4)
for the waiver of the DRE trial
burn.
When
the DRE trial burn is not waived
under Section 726.204(a) (4). each set of
operating requirements must specify the
composition
of
the
hazardous
waste
(including
acceptable
variations
in
the
physical
and
chemical properties of the hazardous waste
which will not affect compliance with the DRE
performance standard) to which the operating
requirements apply.
For each such hazardous
waste, the permit must specify acceptable
operating limits including, but not limited
to, the following conditions as appropriate:
j)
Feed
rate
of
hazardous
waste
and
other
fuels measured and specified as
prescribed
in
subsection
Ce) (6)
Lii
Minimum
and
maximum
device
production
rate when producing normal Product
expressed in appropriate units, measured
and specified as prescribed in
subsection
(e) (6);
iii) ApPropriate controls of the hazardous
waste firing system:
jyj
Allowable variation in BIF system desicm
or
operating
procedures:
128—67 6
207
yj
Minimum combustion gas temperature
measured at a location indicative of
combustion chamber temperature, measured
and specified as prescribed, in
subsection
(e) (6)
yj,1
An appropriate indicator of combustion
gas velocity, measured and specified as
prescribed in subsection
(e) (6). unless
documentation is provided under 35 Ill.
Adm.
Code 703.232 demonstrating adequate
combustion gps residence time;
and
vii) Such other operating requirements as are
necessary to ensure that the DRE
performance standard of Section
726.204(a)
is
met.
~j
CO and hydrocarbon
(HC)
standards.
The
permit
must
incorporate
a
CO
limit
an&
as
appropriate,
a NC limit as provided by
Section 726.204(b).
(c),
(d).
(e)
and
(f).
The permit limits must be specified as
follows:
Li
When complying with the CO standard of
Section 726.204(b) (1). the permit limit
is 100 ppmv
jj)
When com~lvingwith the alternative CO
standard under Section 726.204(c), the
permit limit for CO is based on the
trial burn and is established as the
average over all valid runs of the
highest hourly rolling average CO level
of each run; and, the permit limit for
NC_is_20 ppmv
(as defined in Section
726.204(c) (1)).
except as provided in
Section 726.204(f).
iii) When com~1yjngwith the alternative HC
limit for industrial furnaces under
Section 726.204(f).
the permit limit for
HC and CO is the baseline
level
when.
hazardous waste is not burned as
specified by that subsection.
QJ
Start-up and shut-down.
During start-up and
shut—down of the BIF, hazardous waste except
waste fed solely as an ingredient under the
Tier I
(or adjusted Tier
I)
feed rate
screening limits for metals and
128—677
208
chloride/chlorine, and except low risk waste
exempt
from
the
trial
burn
requirements
under
Sections
726.204(a)
(5),
726.205,
726.206
and
726.207) must not be fed into the device
unless the device is operating within the
conditions of operation specified in the
permit.
21
Requirements to ensure conformance with the
particulate matter
(PM)
standard.
~j
Except
p~
provided in subsections
(e) (3) (B)
and
(C), the permit must specify the
following operating requirements to ensure
conformance
with
the
PM
standard
specified
in
Section
726.205:
11
Total ash feed rate to the device from
hazardous waste,
other fuels and
industrial furnace feedstocks. measured
and specified as prescribed in
subsection
(e) (6)
jjJ
Maximum device production rate when
producing normal product expressed in
appropriate units, and measured and
specified as prescribed jn subsection
(e) (6):
iii) A~pro~riatecontrols on operation and
maintenance of the hazardous waste
firing system and any air pollution
control sYstem (APCS)
jy)
Allowable variation in BIF system design
including any APCS or operating
procedures;
and
yj
Such other operating requirements as are
necessary to ensure that the PM standard
in Section 726.211(b)
is met.
~
Permit conditions to ensure conformance with
the PM standard must not be provided for
facilities exemPt from the PM standard under
Section 726.205(b)
~
For
cement
kilns
and
light-weight
aggregate
kilns. permit conditions to ensure com~1iance
with
the
PM
standard
must
not
limit
the
ash
content of hazardous waste or other feed
materials.
128—678
209
j)
Requirements to ensure conformance with the metals
emissions standard.
~
For conformance with the Tier
I
(or adjusted
Tier I) metals feed rate screening limits of
subsections
(b) or
Ce)
of Section 726.206.
the permit must specify the following
operating requirements:
Li.
Total feed rate of each metal in
hazardous waste, other fuels and
industrial furnace feedstocks measured
and specified under provisions of
subsection
(e) (6):
iii.
Total feed rate of hazardous waste
measured and specified as prescribed in
subsection
(e) (6);
iii)
A
sampling
and
metals
analysis
program
for the hazardous waste,
other fuels and
industrial furnace feedstocks:
~j.
For conformance with the Tier II metals
emission rate screening limits under Section
726.206(c)
and the Tier III metals controls
under Section 726.206(d), the permit must
specify the following operating requirements:
Li
Maximum emission rate for each metal
specified as the average emission rate
during the trial burn
ii!
Feed rate of total hazardous waste and
pum~ablehazardous waste,
each measured
and specified as prescribed in
subsection
(e) (6) (A);
iii)
Feed
rate
of
each
metal
in
the
following
feedstreams.
measured
and
specified
as
prescribed
in
subsections
(e)’(6):’
total
feed
streams;
total
hazardous
waste
feed:
,
and
total
~um~able
hazardous
waste
feed
i~1.
Total
feed
rate
of
chlorine
and
chloride
in
total
feed
streams
measured
and
specified
as
prescribed
in
subsection
(e) (6):
128—679
210
yj
Maximum combustion gas temperature
measured
at
a
location
indicative
of
combustion chamber temperature. and
measured and specified as prescribed in
subsection
(e) (6)
yji
Maximum flue gas temperature at the
inlet to the PM APCS measured and
specified as prescribed in subsection
(e) (6);
vii) Maximum device production rate when
producing normal product expressed in
appropriate units and measured and
specified as prescribed in subsection
Ce) (6);
viii)
Appropriate
controls
on
operation
and maintenance of the hazardous
waste firing system and any APCS
J~j
Allowable variation in BIF system design
including any APCS or operating.
procedures;
and
~
Such
other
operating
requirements
as
are
necessary to ensure that the metals
standards under Sections 726.206(c)
or
Cd)
are met.
Qj
For
conformance
with
an
alternative
implementation a~~roacha~~roved
by the
Agency under Section 726.206(f),
the permit
must specify the following operating
requirements:
Li
Maximum emission rate for each metal
specified as the average emission rate
‘during the trial burn
iii
Feed rate of total hazardous waste and
puinpable hazardous waste. each measured
and specified as prescribed in
subsection
Ce) (6) (A);
iii)
Feed rate of each metal in the following
feedstreams, measured and specified as
prescribed in subsection
(e) (6):
total
hazardous waste feed;
and total
pumpable hazardous waste feed:
128—680
211
jyj
Total feed rate of chlorine and chloride
in total feed streams measured and
specified prescribed in subsection
(e) (6):
ii.
Maximum combustion gas temperature
measured at a location indicative of
combustion
chamber
temperature, and
measured
and
specified
as
prescribed
in
subsection
Ce) (6)
~ji
Maximum
flue
gas
temperature
at
the
inlet to the PM APCS measured and
specified as prescribed in subsection
(e) (6);
vii) Maximum device production rate when
producing normal product expressed in
appropriate units and measured and
specified as prescribed in subsection
(e) (6):
viii)
Appropriate controls on operation
and maintenance of the hazardous
waste firing system and any APCS
j~ç~Allowable variation in BIF system design
including any APCS or operating
procedures,:
and
2c1
Such other operating requirements as are
necessary to ensure that the metals
standards under Sections 726.206(c)
or
(d) are met.
~j
Requirements to ensure conformance with the HC1
and chlorine gas standards.
~
For
conformance
with
the
Tier
I
total
chlorine and chloride feed rate screening
limits of SectiOn 726.207(b) (1). the permit
must specify the following operating
requirements:
Li
Feed rate of total chlorine and chloride
in hazardous waste,
other fuels and
industrial furnace feedstocks measured
and specified as prescribed in
subsection
(e) (6):
128—681
212
.jJJ
Feed rate of total hazardous waste
measured and specified as prescribed in
subsection
(e) (6);
iii) A sampling and analysis program for
total chlorine and chloride for the
hazardous waste1 other fuels and
industrial furnace feedstocks
~1
br conformance with the Tier II HC1 and
chlorine gas emission rate screening limits
under Section 726.207(b) (2) and the Tier III
HCI and chlorine gas controls under Section
726.207(c),
the permit must specify the
following operating requirements:
iL
Maximum emission rate for HC1 and for
chlorine gas specified as the average
emission rate during the trial burn
jjJ
Feed rate of total hazardous waste
measured and specified as prescribed in
subsection
(e) (6):
iii) Total feed rate of chlorine and chloride
in total feed streams1 measured and
specified as prescribed in subsection
(e) (6)
i~1
Maximum device production rate when
producing normal product expressed in
appropriate units, measured and
specified as prescribed in subsection
(e) (6)
~j
Appropriate controls on operation and
maintenance of the hazardous waste
firing system and any APeS:
~il
Allowable variation in BIF system design
including any APCS or operating
procedures;
and
vii) Such other operating re~uirementsas are
necessary to ensure that the HC1 and
chlorine gas standards under Section
726.207(b) (2)
or
(C)
are met.
~j
Measuring parameters and establishing limits based
on trial burn data.
128—682
213
~
General requirements.
As specified in
subsections
(e) (2) through
(e) (5)
•
each
operating parameter must be measured. and
permit limits on the parameter must be
established, according to either of the
following procedures:
j).
Instantaneous limits.
A Parameter
~S
measured and recorded on an
instantaneous basis
(i.e., the value
that occurs at any time)
and the permit
limit specified as the time-weighted
average during all valid runs of the
trial burn;
or
JJJ~ Hourly rolling average.
The limit for a
parameter must be established and
continuously monitored on an hourly
rolling average basis, as defined in
Section 726.200(g).
The permit
limit
for the parameter must be established
based on trial burn data as the average
over all valid test runs of the highest
hourly rolling average value for each
run.
P1
Rolling average limits for carcinogenic
metals and lead.
Feed rate limits for the
carcinogenic metals
(as defined in Sectiofl
726.200(g))
and lead must be established
either on an hourly rolling average basis as
prescribed bY subsection
(e) (6) (A) or on (up
to)
a 24 hour rolling average basis.
If the
owner or operator elects to use an average
period from 2 to 24 hours:
fl.
The feed rate of each metal must be
limited at any time to ten times the
feed rate that would be allowed on an
hourly rolling average basis
jjj
Terms
are as defined in Section
726.200(g); and
liii The permit limit for the feed rate of
each metal must be established based on
trial burn data as the average over all
valid test runs of the highest hourly
rolling average feed rate for each run.
~j
Feed rate limits for metals, total chlorine
and chloride, and ash.
Feed rate limits for
128—683
214
metals,
total chlorine and chloride, and ash
are established and monitored by knowing the
concentration of the substance
(i.e., metals.
chloride/chlorine
and
ash)
in each feedstream
and the flow rate of the feedstream.
To
monitor the feed rate of these substances,
the flow rate of each feedstreain must be
monitored under the continuous monitoring
requirements of subsections
(e) (6) (A) and
(B).
pj~.
Conduct of trial burn testing.
j~.
If compliance with all applicable
emissions standards of Sections 726.204
through 726.207 is not demonstrated
simultaneously during a set of test
runs, the operating conditions of
additional test runs required to
demonstrate com~1iancewith remaining
emissions standards must be as close as
possible to the original operating
conditions.
jjj.
Prior to obtaining test data for
purposes of demonstrating compliance
with the emissions standards of Sections
726.204 through 726.207 or establishing
limits on operating parameters under
this Section. the unit must operate
under trial burn conditions for a
sufficient period to reach steady-state
operations.
However, industrial
furnaces that recycle collected PM back
into the furnace and that comply with an
alternative implementation approach fot~
metals under Section 726.206(f) need not
reach steady state conditions with
respect to the flow of metals in the
system prior to beginning compliance
testing for metals emissions.
iii) Trial burn data on the level of an
operating parameter for which a limit
must be established in the permit must
be obtained during emissions sampling
for the pollutant(s)
(i.e.. metals.
PM.
HC1/chlorine gas. organic compounds)
for
which the parameter must be established
as specified by subsection
(e).
fl
General requirements.
128—684
215
~
Fugitive emissions.
Fugitive emissions must
be controlled by:
il
Keeping the combustion zone totally
sealed against fugitive emissions;
or
ja
Maintaining the combustion zone pressure
lower than atmospheric oressure;
or
iii)
An alternate means of control
demonstrated
(with
Part
B
of
the
permit
application)
to
provide
fugitive
emissions
control
eauivalent
to
maintenance of combustion zone pressure
lower than atmospheric pressure.
P1
Automatic waste feed cutoff.
A BIF must be
operated with a functioning system that
automatically cuts off the hazardous waste
feed when operating conditions deviate from
those established under this Section.
In
addition:
jj
The permit limit for (the indicator of)
minimum combustion chamber temperature
must be maintained while hazardous waste
or hazardous waste residues remain in
the combustion chamber,
~JJ
Exhaust Qases must be ducted to the APCS
operated in accordance with the permit
requirements while hazardous waste or
hazardous waste residues remain in the
combustion chamber;
and
iii) Operating parameters for which permit
limits are established must continue to
be monitored during the cutoff. and the
hazardous waste feed must not be
restarted until the levels of those
parameters complY with the ~érmi?
limits.
For parameters that are
monitored on an instantaneous basis, the
Agency shall establish a minimum period
of time after a waste feed cutoff during
which the parameter must not exceed the
permit limit before the hazardous waste
feed is restarted.
~j
Changes.
A BIF must cease burning hazardous
waste when combustion properties,
or feed
128—685
216
rates of the hazardous waste, other fuels or
industrial furnace feedstocks, or the BIF
design or operating conditions deviate from
the limits as specified in the permit.
Pj.
Monitoring and Inspections.
~
The owner or operator shall monitor and
record the following, at a minimum, while
burning hazardous waste:
LL
If specified by the permit, feed rates
and composition of hazardous waste.
other fuels and industrial furnace
feedstocks,
and feed rates of ash,
metals and total chlorine and chloride:
£iJ.
If specified by the permit,
CO. HCs
and
oxvaen on a continuous basis at a common
point in the BIF downstream of the
combustion zone and prior to release of
stack gases to the atmosphere in
accordance with operating requirements
specified in subsection
(e) (2) (8).
CO.
HC and oxygen monitors must be
installed,
operated and maintained in
accordance with methods specified in
Appendix
I
(“eye”).
iii) Upon the reauest of the Agency, sampling
and analysis of the hazardous waste (and
other fuels and industrial furnace
feedstocks as appropriate). residues and
exhaust emissions must be conducted to
verify that the operating requirements
established in the permit achieve the
applicable standards of Sections
726.204,
726.205. 726.206 and 726.207.
~j
All monitors must record data in units
corresponding to the permit limit unless
otherwise specified in the permit.
~j.
The BIF and associated equipment (pumps.
values,
pipes, fuel storage tanks.
etc.) must
be subiected to thorough visual inspection
when it contains hazardous waste,
at least
daily for leaks, spills, fugitive emissions
and signs of tampering.
Qj
The automatic hazardous waste feed cutoff
system and associated alarms must be tested
128—686
217
at least once everY
7 days when hazardous
waste is burned to verify operability, unless
the applicant demonstrates to the Aaency that
weekly inspections will unduly restrict or
upset operations and that less frequent
inspections will be adequate.
At a minimum.
operational testina must be conducted at
least once every 30 days.
~
These monitorina and inspection data must be
recorded and the records must be placed in
the o~eratin~record required by 35 Ill. Adm.
Code 724.173.
~
Direct transfer to the burner.
If hazardous waste
is directly transferred from a transPort vehicle
to
a BIF without the use of a storaae unit, the
owner and operator shall com~lvwith Section
726.211.
~Qj
Recordkeepina.
The owner or operator shall keep
in the operating reôord of the facility all
information and data required by this Section
until closure of the facility.
~
Closure.
At closure, the owner or operator shall
remove all hazardous waste and hazardous waste
residues
(including, but not limited to. ash,
scrubber waters and scrubber sludges) from the
BIF.
(Source:
Added at 16 Iii.
Reg.
,
effective
)
Section 726.203
Interim status standards for Burners
~j
PurPose. scope, a~~1icabilitv.
~j
General.
~j
The purpose of this Section is to establish
minimum
national standards for owners and
oPerators of “existing” BIFs that burn
hazardous waste where such standards define
the acceptable management of hazardous waste
during the oerlod of interim status.
The
standards of this Section a~~1y
to owners and
operators of existina facilities until either
a permit is issued under Section 726.202(d)
or until closure responsibilities identified
in this Section are fulfilled.
128—687
218
P1
“Existing” or “in existence” means a BIF that
on or before August 21.
1991
is either in
operation burning or processing hazardous
waste or for which construction (including
the ancillary facilities to burn or to
process the hazardous waste)
has commenced.
A facility has commenced construction
if the
owner or operator has obtained the federal.
State and local approvals or permits
pecessary to begin ~hvsica1 construction
and either:
jj
A continuous on-site, ~hysica1
construction Program has begun;
or
LU..
The owner or operator has entered into
contractual obligations, which cannot be
canceled or modified without substantial
loss,
for physical construction of the
facility to be completed within a
reasonable time.
Qj
If a BIF is located at a facility that
already has a RCRA permit or interim status,
then the owner or operator shall comply with
the applicable reaulations dealing with
permit modifications in 35 Ill. Adm. Code
703.280 or changes in interim status in 35
Ill. Adm. Code 703.155.
~
Exemptions.
The requirements of this Section do
not apply to hazardous waste and facilities exempt
under Sections 726.200(b)
or 726.208.
~
Prohibition on burning dioxin-listed wastes.
The
following hazardous waste listed for dioxin and
hazardous waste derived from any of these wastes
must not be burned in a BIF operating under
interim status:
USEPA Hazardous Waste Numbers
F020, F021.
F022. F023.
F026 and F027.
j)
Applicability of
35 Iii. Adm. Code 725 standards.
Owners and operators of BIFs that burn hazardous
waste and are operating under interim status are
subiect to the following provisions of 35 Ill.
Adm. Code 725, except as provided otherwise by
this Section:
~j.. In Subpart A (General),
35 Ill. Adm. Code
725.104:
128—688
219
P1
In Subpart B (General facility standards),
35
Ill. Adm. Code 725.111
—
725.117
Qj.
In Subpart C (Preparedness and prevention).
35
Ill. Adm. Code 725.131
—
725.137
QJ.
In Subpart D (Continaencv plan and emergency
procedures).
35 Ill. Adm. Code 725.151
—
725.1.56
~j
In Subpart E
(Manifest system. recordkeeping
and_reporting),
35 Ill. Adm. Code 725.171
-
725.177. except that 35 Ill. Adm. Code
725.171.
725.172 and 725.176 do not a~plvto
owners and operators of on—site facilities
that do not receive any hazardous waste from
off—site sources
fi
In Subpart G (Closure and post-closure),
35
Ill.
Adm. Code 725.211
—
725.215
Qj
In Subpart H (Financial requirements).
35
Ill. Adm. Code 725.241,
725.242,
725.243 and
725.247
-
725.251.
except that the State of
Illinois and the Federal government are
exempt from the requirements of
35
Ill.
Adin.
Code 725.Subpart H:
and
111
Subpart BB (Air emission standards for
equipment leaks). except 35 Ill. Adm. Code
725.950(a).
~j
Special requirements for furnaces.
The following
controls a~~lvduring interim status to industrial
furnaces (e.g.,
kilns, cupolas) that feed
hazardous waste for a purpose other than solely as
an_ingredient
(see subsection (a)(5)(B))
at any
location other than the hot end where products are
normally discharged or where fuels are normally
fired:
~j.
Controls.
j)
The hazardous waste must be fed at
a.
location where combustion gas
temperatures are at least 1800 °F
iii
The
owner
or
operator
shall
determine
that
adequate
oxygen
is
present
in
combustion gases to combust organic
constituents in the waste and retain
128—689
220
documentation of such determination in
the facility record;
iii) For cement kiln systems. the hazardous
waste must be fed into the kiln;
and
jyj
The HC controls of Section 726.204(f)
or
subsection
(c) (5)
apply upon
certification of compliance under
subsection
(C)
irrespective of the CO
level achieved during the compliance
test.
P1
Burning hazardous waste solely as an
ingredient.
A hazardous waste is burned for
a purpose other than “solely as an
ingredient”
if it meets either of these
criteria:
LL
The hazardous waste has a total
concentration of nonmetal compounds
listed in 35
Ill. Adm. Code 721.Appendix
H. exceeding 500 ~pm by weight,
as fired
and so is considered to be burned for
destruction.
The concentration of
nonmetal compounds in a waste as—
generated may be reduced to the 500 ppm
limit by bona tide treatment that
removes or destroys nonmetal
constituents.
Blending for dilution to
meet the 500 ppm limit is prohibited and
documentation that the waste has not
been impermissibly diluted must be
retained in the facility record;
or
£JJ..
The hazardous waste has a heating value
of_5.000 Btu/lb or more,
as fired,
and
so is considered to be burned as fuel.
The heating value of a waste as—
generated may be reduced to below the
5.000 Btu/lb limit by bona tide
treatment that removes or destroys
organic constituents.
The heating value
of a waste as—generated may be reduced
to below the 5.000 Btu/lb limit by bona
tide treatment that removes or destroys
organic constituents.
Blending to
augment the heating value to meet the
5,000 Btu/lb limit is prohibited and
documentation that the waste has not
been inipermissibly blended must be
retained in the facility record.
128—690
221
~j
Restrictions on burning hazardous waste that is
not a fuel.
Prior to certification of compliance
under subsection
(C), owners and operators shall
not feed hazardous waste that has a heating value
less than 5000 BtuJlb,. as generated.
(except that
the heating value of a waste as—generated may be
increased to above the~5.000 Btu/lb limit by bona
fide treatment:
however
.
blending to augment the
heating value to meet the 5,000 Btu/lb limit is
prohibited and records itust be kept to document
that impermissible blending has not occurred)
in a
BIF. except that:
~j.
Hazardous waste may be burned solely as an
ingredient;
or
p1
Hazardous waste may be burned for purposes of
compliance testing (or testing prior to
compliance testing) for a total period of
time not to exceed 720 hours;
or
~j
Such waste may be burned if the A~encvhas
documentation to show that,
prior to August
21~ 1991:
fl.
The BIF was operating under the interim
status standards for incinerators or
thermal treatment units.
35 Ill. Adm.
Code 725.Subparts 0 or P;
and
jiJ
The BIF met the interim status
eligibility requirements under 35 Ill.
Adni. Code 703.153 for 35 Ill. Adm. Code
725.Subparts 0 or P;
and
iii) Hazardous waste with a heating value
less than 5.000 Btu/lb was burned prior
.to that date;
or
~j
Such waste may be burned in a halogen acid
furnace if the waste was burned as an
excluded ingredient under 35 Ill. Adm. Code
721.102(e)
prior to February 21.
1991, and
documentation is kept on tile supporting this
claim.
fl
Direct transfer to the burner.
If hazardous waste
is directly transferred from a transport vehicle
to a BIF without the use of a storage unit,
the
owner and operator shall comply with Section
726.211.
128—69 1
222
Certification of precom~liance.
fl..
The Board incorporates by reference 40 CFR
266.
103(b);
adopted at 56 Fed.
Req.
7206.
February
21.
1991;
56
Fed.
Req.
32688.
July 17,
1.991;
arid
56
Fed
Rep.
42511.
August
27.
1991.
This
Section
incorporates
no
later
editions
or
amendments.
21
Certain
owners
and
operators
were
required to file
a certification of ~recomp1iance with USEPA by
August 21.
1991, pursuant to 40
CER
266.103(b).
No separate filing is required with the Agency.
~j.
Certification of compliance.
The owner or operator
shall conduct emissions testing to document compliance
with the emissions standards of Sections 726.204(b)
through
(e). 726.205, 726.206,
726.207. and subsection
(a) (5) (A) (iv). under the procedures prescribed by this
subsection, except under extensions of time provided by
subsection
(c) (7).
Based on the compliance test, the
owner or operator shall submit to the Agency, on or
before August 21,
1992. a complete and accurate
“certification of compliance”
(under subsection
(c)(41)
with those emission standards establishing limits on
the operating parameters specified in subsection
(C)
(1).
~
Limits on operating conditions.
The owner or
operator shall establish limits on the following
parameters based on operations during the
compliance test (under procedures prescribed in
subsection
(c)(4)(D))
and include these limits
with the certification of compliance.
The BIF
must be operated in accordance with these
operating limits and the applicable emissions
standards of Section 726.204(b)
—
(e), 726.205.
726.206, 726.207 and subsection
(a) (5) (A) (iv) at
all times when there is hazardous waste in the
unit.
~j
Feed rate of total hazardous waste and
(unless complying the Tier I or adiusted Tier
I metals feed rate screenIng limits under
Section 726.206(b)
or
(efl,
~umpab1e
hazardous waste:
p1
Feed rate of each metal in the following
feedstreanis:
j).
Total feedetreams, except that
industrial furnaces that must comply
128—692
223
with the alternative metals
implementation approach under subsection
(c) (3) (B) must specify limits on the
concentration of each metal in collected
PM in lieu of feed rate limits for total
feedstreams:
.jjj..
Total hazardous waste feed
(unless
complying with the Tier I or adjusted
Tier I metals feed rate screening limits
under Section 726.206(b)
or
(efl;
and
iii) Total pum~ablehazardous waste feed.
~
Total feed rate of total chlorine and
chloride in total feed streams
~j
Total feed rate of ash in total feed streams,
except that the ash feed rate for cement
kilns and light-weight aa~reaatekilns
is not
limited
p1
Co concentration, and where required, HC
concentration in stack gas.
When complying
with the CO controls of Section 726.204(b).
the CO limit is 100 ppmv, and when complying
with the HC controls of Section 726.204(c).
the HC limit is 20
ppniv.
When complying with
the CO controls. of Section 726.204(c). the CO
limit is established based on the compliance
test
p1
Maximum production rate of the device in
a~pro~riateunits when producing normal
product
~j
Maximum combustion chamber temperature where
the temperature measurement is as close to
the_combustion zone as possible and is
upstream of any auench water injection,
(unless complyina with the Tier I adjusted
Tier I metals feed rate screening limits
under Section 726.206(b)
or (e))
p1
Maximum flue gas temperature entering a PM
control device (unless complying with Tier I
or adjusted Tier
I metals feed rate screening
limits under Section 726.206(b)
or (e))
fl
For systems using wet scrubbers.
including
wet ionizing scrubbers
(unless complying with
the Tier I or adiusted Tier
I metals feôd
128—693
224
rate screening limits under Section
726.206(b)
or
(e) and the total chlorine and
chloride feed rate screening limits under
Section 726.207(b) (1)
or
(efl:
jJ
Minimum liauid to flue aas ratio
JJJ.
Minimum scrubber blowdown from the
system or maximum suspended solids
content of scrubber water:
and
iii) Minimum PH level of the scrubber water
~j
For systems usina venturi scrubbers. the
minimum differential gas pressure across the
venturi
(unless com~l.yinqthe Tier
I or
adjusted Tier I metals feed rate screening
limits under Section 726.206(b) or
(e) and
the total chlorine and chloride feed rate
screening limits under Section 726
•
207 (b) (1)
or
(e)).
~
For systems using dry scrubbers
(unless
com~1yinqwith the Tier I or adiusted Tier I
metals feed rate screening limits under
Section 726.206(b) or
(e) and the total
chlorine and chloride feed rate screening
limits under Section 726.207(b) (1) or (e)):
jj..
Minimum caustic feed rate;
and
jjJ.
Maximum flue gas flow rate:
~
For systems using wet ionizing scrubbers or
electrostatic precipitators
(unless complying
with the Tier
I or adjusted Tier I metals
feed rate screening limits under Section
726.206(b) or
(e)
and the total chlorine and
chloride feed rate screening limits under
Section 726.207(b) (1) or
(efl:
fl
Minimum electrical power in kVA to the
precipitator plates:
and
jj1.
Maximum flue aas flow rate
~fj
For systems using fabric filters
(baghousesi..
the minimum Pressure drop (unless complying
with the Tier I or adiusted Tier I metals
feed rate screening limits under Section
726.206(b) or
(e)
and the total chlorine and
128—694
225
chloride feed rate screening limits under
Section 726.207(b) (1)
or
(efl.
21
Prior notice of compliance testing.
At least 30
days prior to the compliance testing required by
subsection
(cI(3). the owner or oPerator shall
notify the AQency and submit the following
information:
~j.. General facility information including:
iL
USEPA facility ID number
iSJ
Facility name. contact person. telephone
number and address;
iii) Person responsible for conducting
compliance test. including company name,
address and telephone number,
and a
statement of qualifications
jyj
Planned date of the compliance test:
Specific
information on each device to be
tested including:
LL
Description of BIF
JJJ..
A scaled clot plan showing the entire
facility and location of the BIF;
iii) A description of the APCS
jyj..
Identification of the continuous
emission monitors that are installed,
including:
CO monitor;
Oxygen
monitor;
HC monitor. specifvin~the
minimum temperature of the system and,
-if the temperature is less than 150
°C,
an exi,lanation of why a heated system is
not used (see subsection
(c)(5)) and a
brief description of the sample gas
conditioning system
yl
Indication of whether the stack is
shared with another device that will be
in operation during the compliance test
iii
Other information useful to an
understanding of the system design or
operation.
128—695
226
Q1
Information on the testing planned, including
a complete copy of the test protocol and
QA/OC plan. and a summary description for
each test providing the following information
at a minimum:
il
Purpose of the test (e.g.. demonstrate
compliance with emissions of PM);
and
uI
Planned operating conditions.
including
levels for each pertinent parameter
specified in subsection
(C)
(1).
21
Compliance testing.
~
General.
Compliance testing must be.
conducted under conditions for which the
owner or operator has submitted a
certification of ~recompliance under
subsection
(b) and under conditions
established in the notification of compliance
testing required by subsection
(c) (2).
The
owner or operator may seek approval on a
case—by-case basis to use compliance test
data from one unit in lieu of testing a
similar on-site unit.
To support the
request. the owner or operator shall provide
a cpm~arisonof the hazardous waste burned
and other feedstreains, and the design.
operation,
and maintenance of both the tested
unit and the similar unit.
The Agency shall
provide a written approval to use compliance
test data in lieu of testing a similar unit
if the Agency finds that the hazardous
wastes, devices and the operating conditions
are sufficiently similar, and the data from
the other compliance test is adequate to meet
the requirements of subsection
(c).
p1
Special requirements for industrial furnaces
that recycle collected PM.
Owners and
operators of industrial furnaces that recycle
back into the furnace PM
from the APCS shall
comply with one of the following procedures
for testing to determine compliance with the
metals standards of Section 726.206(c)
or
(d):
fl
The special testing requirements
prescribed in “Alternative Method for
Implementing Metals Controls” in
Appendix
I
(“eye”):
or
128—696
227
jjj
Stack emissions testing for a minimum of
6 hours each day while hazardous waste
is burned during interim status.
The
testing must be conducted when burning
normal hazardous waste for that day at
normal feed rates for that day and when
the APCS is operated under normal
conditions.
During interim status,
hazardous waste analysis for metals
content must be sufficient for the- owner
or_operator to determine if chanaes in
metals content affect the ability of the
unit to meet the metals emissions
standards established under Section
726.206(c) or
(d).
Under this option.
operating limits
(under subsection
(c) (1)) must be established during
compliance testing under subsection
(c) (3) only on the following parameters:
Feed rate of total hazardous waste;
Total feed rate of total chlorine and
chloride in total feed streams;
Total
feed rate of ash in total feed streams,
except that the ash feed rate for cement
kilns and light-weight aggregate kilns
is not limited;
CO concentration. and
where required, MC concentration in
stack gas;
Maximum production rate of
the device in approPriate units when
producing normal product;
or
iii) Conduct compliance testing to determine
compliance with the metals standards to
establish limits on the operatin~
parameters of subsection
(c) (1) onlY
after the kiln system has been
conditioned to enable it to reach
equilibrium with respect to metals fed
into_the system and metals emissions.
During conditioning, hazardous waste and
raw materials having the same metals
content as will be fed during the
compliance test must be fed at the feed
rates that will be fed during the
compliance test.
ci
Conduct of compliance testing.
If
compliance with all applicable
emissions standards of Sections 726.204-
through 726.207
is not demonstrated
128—69 7
228
simultaneously during a set of test
runs,
the operating conditions of
additional test runs required to
demonstrate compliance with remaining
emissions standards must be as close as
possible to the original operating
conditions.
JJJ
Prior to obtaining test data for
purposes of demonstrating compliance
with the applicable emissions standards
of Sections 726.204 through 726.207 or
establishing limits on operating
parameters under this Section. the
facility must operate under compliance
test conditions for a sufficient period
to reach steady—state operations.
Industrial furnaces that recycle
collected PM back into the furnace and
that comply with subsections
(c) (3) (B)
(i)
or
(ii).
however, need not
reach steady state conditions with
respect to the flow of metals in the
system prior to beginning compliance
testing for metals.
iii) Compliance test data on the level of an
operating parameter for which a limit
must be established in the certification
of compliance must be obtained during
emissions sampling for the pollutant(s)
(i.e.. metals. PM. Mci/chlorine gas.
organic compounds)
for which the
parameter must be established as
specified by subsection
(c) (1).
4j.
Certification of compliance.
Within 90 days of
com~ietingcompliance testing, the owner or
pp~ratorshall certify to the Agency compliance
with the emissions standards of Sections
726.204(b),
(c) and (el, 726.205.
726.206,
726.207. and subsection
(a) (5) (A) (iv).
The
certification of compliance must include the
following information:
~
General facility and testing information
including:
j)..
USEPA facility ID number:
jjJ
Facility name, contact person. telephone
number and address
128—698
229
iii) Person responsible for conducting
compliance testing. including com~anv
name, address and telephone number,
and
a statement of qualifications
jy).
Date(s) of each compliance test
~i
Description of BIF tested
yfl.
Person res~ons1blefor QA/OC. title and
telePhone number, and statement that
procedures prescribed in the QA/QC ~ian
submitted under Section 726.203 (ci (2) (C)
have been followed,
or a description of
any changes and an explanation of.whv
changes were necessary.
vii) Description of any chan~esin the unit
configuration prior to or during testing
that would alter any of the information
submitted in the prior notice of
compliance testing under subsection
(C)
(2). and an explanation of why the
chan~eswere necessary;
viii)
Description of any changes in the
planned test conditions prior to or
during the testing. that alter any
of the information submitted in the
prior notice of compliance testing
under subsection
(ci (2). and an
explanation of why the changes were
necessary:
and
j?çj
.The complete report on results of
emissions testing.
p1
Specific information on each test including:
LL
PurPose(s) of test
(e.g.. demonstrate
conformance with the emissions limits
for PM. metals, MCi. chlorine gas and
cQi
jJJ
Summary of test results for each run and
for each test including the following
information:
Date of run;
Duration
of run;
Time—weighted averaae and
highest hourly rolling averaPe CO level
for each run and for the test;
Highest
hourly rolling avera~eMC level,
if MC
128—699
230
monitoring is required for each run and
for the test:
If dioxin and furan
testing is required under Section
726.204(e). time—weighted average
emissions for each run and for the test
of chlorinated dioxin and furan
emissions, and the predicted maximum
annual average ground level
concentration of the toxicity
equivalency factor
(defined in Section
726
•
200(g));
Time—weighted average PM
emissions for each run and for the test;
Time-weighted average HC1 and chlorine
gas emissions for each run and for the
test;
Time—weighted averaPe emissions
for the metals subject to regulation
under Section 726.206 for each run
arid
for the test;
and QA/OC results.
çj
Comparison of the actual emissions during
each test with the emissions limits
prescribed by Sections 726.204(b).
(c) and
(e). 726.205.
726.206 and 726.207 and
established for the facility in the
certification of ~recomn~lianceunder
subsection
(bi.
fli
Determination of operating limits based on
all valid runs of the compliance test for
each applicable parameter listed in
subsection
(c) (1) using either of the
following procedures:
j)
Instantaneous limits.
A parameter must
be measured and recorded on an
instantaneous basis
(i.e.. the value
that occurs at any time) and the
operating limit specified as the time-
weiahted average during all runs of the
compliance test;
or
jjj.
Hourly rolling average basis..
The limit
for a parameter must be established and
continuously monitored on an hourly
rolling average basis.
as defined in
Section 726.200(g).
The operating limit
for the parameter must be established
based on compliance test data as the
average over all test runs of the
highest hourly rolling average value for
each run.
128—700
231
iii) Rolling average limits for carcinogenic
metals and lead.
Feed rate limits for
the carcinogenic metals and lead must be
established either on an hourly rolling
average basis as prescribed by
subsection
(c) (4) (DI (ii) or on (u~to)
a
24 hour rolling average basis.
If the
owner or operator elects to use an
averaging period from
2 to 24 hours:
The feed rate of each metal must be
limited at any time to ten times the
feed_rate that would be allowed on a
hourly rolling averaae basis;
The
continuous monitor is as defined in
Section 726.200(g).
And the operating
limit for the feed rate of each metal
must be established based on compliance
test data as the average over all test
runs of the highest hourly rolling
average feed rate for each run.
iii.
Feed rate limits for metals, total
chlorine and chloride and ash.
Feed
rate limits for metals. total chlorine
and chloride and ash are established and
monitored by knowing the concentration
of the substance
(i.e.. metals,
chloride/chlorine and ash)
in each
feedstream and the flow rate of the
feedstream.
To monitor.the feed rate of
these substances,
the flow rate of each
feedstream must be monitored under the
continuous monitoring requirements of
subsections
(c)(4)(D)(i) throuah
(iii).
p1
Certification of compliance statement.
The
following statement must accompany the
certification of compliance:
“I certify under penalty of law that this
information was PrePared under mY direction
or suPervision in accordance with a system
designed to ensure that qualified personnel
properly aathered and evaluated the
information
and
supporting
documentation.
Copies of all emissions tests.
dispersion
modeling results and other information used
to determine conformance with the
requirements of 35 Ill. Adm. Code 726.203(c)
are available at the facility and can be
obtained from the facility contact person
listed above.
Based onmny inquiry of the
128—701
232
person or persons who manages the facility,
or those persons directly responsible for
gathering the information, the information
submitted is. to the best of my knowledge and
belief, true,
accurate and complete.
I am
aware that there are significant penalties
for submitting false information, including
the possibility of fine and imprisonment- for
knowing violations.
I also acknowledge that the operating limits
established pursuant to 35 Ill. Adm. Code
726.203(c) (4) (DI are enforceable limits at
which the facility can le~allvoperate during
interim status until a revised certification
of compliance is submitted.”
~j.
Special requirements for MC monitoring systems.
When an owner or operator is required to com~lv
with the MC controls provided by Sections
726.204(c)
or subsection
(a) (5) (A) (iv).
a
conditioned gas monitoring system may be used in
conformance with specifications provided in
Appendix I
(“eve”) provided that the owner or
operator submits a certification of compliance
without using extensions of time provided by
subsection
(ci (7).
~j
Special operatina requirements for industrial
furnaces that recycle collected PM.
Owners and
operators of industrial furnaces that recycle back
into the furnace PM
from the APCS must:
~j
When complying with the requirements of
subsection
(ci (3) (B) (ii. com~lvwith the
operating requirements prescribed in
“Alternative Method to Implement the Metals
Controls” in Appendix I
(“eve”);
and
p1
When complying with the requirements of
subsection
(ci (3) (B) (ii).
comply with the
operating requirements prescribed by that
subsection.
fl
Extensions of time.
~J
If the owner or operator does not submit a
complete certification of compliance for all
of the applicable emissions standards of
Sections 726.204. 726.205, 726.206 and
726.207 by August 21,
1992.
the owner or
operator shall either:
128—702
233
j)
Stop burning hazardous waste and begin
closure activities under subsection
(1)
for the hazardous waste portion of the
facility;
or
JJJ
Limit hazardous waste burning only for
purposes of compliance testing (and
pretesting to prepare for compliance
testing)
a total period
pf
720 hours for
the period of time beginning Au~st 21.
1992._submit a notification to the
A~encvby Auaust 21.
1992 stating that
the facility is operating under
restricted interim status and intends to
resume burning hazardous waste, and
submit
a complete certification of
compliance bY August 23.
1993:
or
iii) Obtain a case—by—case extension of time
under subsection
(ci (7) (B).
p1
Case—by—case extensions of time.
See Section
726.219.
21
Revised certification of compliance.
The owner or
operator may submit at any time a revised
certification of comoliance
(recertification of
compliance)
under the following procedures:
~j.
Prior to submittal of a revised certification
of compliance, hazardous waste must not be
burned for more than a total of 720 hours
under operating conditions that exceed those
established under a current certification of
compliance,
and such burning must be
conducted only for purposes of determining
whether the facility can operate under
revised conditions and continue to meet the
applicable emissions standards of Sections
726.204. 726.205. 726.206 and 726.207
p1
At least 30 days prior to first burning
hazardous waste under operating conditions
that exceed those established under a current
certification of compliance. the owner or
operator shall notify the Agency and submit
the following information:
£).
USEPA facility ID number, and facility
name,
contact person. telephone number
and address:
128—703
234
jj)
Operating conditions that the owner or
operator is seeking to revise and
description of the changes in facility
design or operation that prompted the
need to seek to revise the operating
conditions;
iii)
A determination that, when operating
under the revised operating conditions.
the_ap~licab1eemissions standards of
Sections 726.204. 726.205, 726.206 and
726.207 are not likely to be exceeded.
To_document this determination, the
owner or operator shall submit the
applicable information required under
subsection
(b) (2);
and
jyj
Complete emissions testing protocol for
any pretesting and for a new compliance
test to determine compliance with the
applicable emissions standards of
Sections 726.204, 726.205.
726.206 and
726.207 when operating under revised
operating conditions.
The protocol
shall include a schedule of pre—testing
and compliance testing.
If the owner
and operator revises the scheduled date
for the compliance test, the owner or
operator shall notify the Agency in
writing at least 30 days prior to the
revised date of the compliance test
ci
Conduct a compliance test under the revised
operating conditions and the protocol
submitted to the Agency to determine
compliance with the applicable emissions
standards of Sections 726.204.
726.205.
726.2.06 and 726.207;
and
~
Submit a revised ceX~tificationof compliance
under subsection
(ci (4).
Periodic
Recertifications.
The owner or operator shall
conduct compliance testing and submit to the Agency a
recertification of compliance under provisions of
subsection
(ci within three years from submitting the
previous certification or recertification.
If the
owner or operator seeks to recertify compliance under
new operating conditions,
the owner or operator shall
comply with the requirements of subsection
(ci (8).
128—7
04
235
~
Noncompliance with certification schedule.
If the
owner or operator does not com~lvwith the interim
status compliance schedule provided by subsections
(b),
(c) and
(di. hazardous waste burnina must terminate on
the date that the deadline is missed, closure
activities must begin under subsection
(1)
•
and
hazardous waste burning must not resume except under an
operating permit issued under 35 Ill. Adm. Code
703.232.
For ~urmoses of compliance with the closure
provisions of subsection
(1) and 35 Ill. Mm. Code
725.212(d) (2) and 725.213 the BIF has received “the
known final volume of hazardous waste” on the date the
deadline is missed.
fj
Start—up and shut—down.
Hazardous waste
(except waste
fed solely as an ingredient under the Tier
I
(or
adjusted Tier
I) feed rate screening limits for metals
and chloride/chlorine) must not be fed into the device
during start—up and shut-down of the BIF. unless the
device is operating within the conditions of operation
specified in the certification of compliance.
gj
Automatic waste feed cutoff.
During the compliance
test required by subsection
(ci (3). and upon
certification of compliance under subsection
(ci. a BIF
must be operated with a functioning system that
automatically cuts off the hazardous waste feed when
the_applicable operating conditions specified in
subsections
(ci (1) (A)
and. (E)
-
(Mi deviate from those
established in the certification of compliance.
In
addition:
il
To minimize emissions of organic compounds. the
minimum combustion chamber temperature
(or the
indicator of combustion chamber temperature) that
occurred during the compliance test must be
maintained while hazardous waste or hazardous
waste residues remain in the combustion chamber.
with the minimum temperature during the compliance
test defined as either:
~
If compliance with the combustion chamber
temperature limit
is.
based
on a hourly
rolling average, the minimum temperature
during the compliance test is considered to
be the average over all runs of the lowest
hourly rolling average for each run;
or
p1
If compliance with the combustion chamber
temperature limit is based on an
instantaneous temperature measurement. the
minimum temperature during the compliance
128—705
236
test is considered to be the time-weighted
average temperature during all runs of the
test;
and
21
Operating parameters limited by the certification
of compliance must continue to be monitored during
the cutoff.
and
the
hazardous
waste
feed
must
not
be
restarted
until
the
levels
of
those
parameters
comply
with
the
limits
established
in
the
certification of com~liance.
~
Fugitive emissions.
Fugitive emissions must be
controlled by:
~
Keeping the combustion zone totally sealed against
fugitive emissions;
or
~j
Maintaining
the
combustion
zone
pressure
lower
than atmospheric pressure:
or
21
An alternate means of control that the owner or
operator demonstrates provides fugitive emissions
control
equivalent
to
maintenance
of
combustion
zone pressure lower than atmospheric pressure.
Support.
f~or
such demonstration must be included in
the operating record.
j)~
Changes.
A BIF must cease burning hazardous waste when
combustion
properties.
or
feed
rates
of
the
hazardous
waste,
other fuels or industrial furnace feedstocks, or
the BIF design or o~eratinaconditions deviate from the
limits specified in the certification of compliance.
jj
Monitoring and Inspections.
fl
The owner or operator shall monitor and record the
following,
at a minimum, while burning hazardous
waste:
~j
Feed
rates
and
composition
of
hazardous
waste,
other
fuels
and
industrial
furnace
feed
stocks,
and
feed
rates
of
ash.,
metals.
and
total
chlorine
and
chloride
as
necessary
to
ensure
conformance
with
the
certification
of
~recomp1jance
or
certification
of
compliance
p1
CC.
oxygen
and, if applicable. MC. on a
continuous
basis
at
a
common
point
in
the
BIF
downstream of the combustion zone and prior
to
release
of
stack
gases
to
the
atmosphere
in accordance with the operatina limits
128—706
237
specified in the certification of compliance.
CO. HC and oxygen monitors must be installed.
operated
and
maintained
in accordance with
methods specified in Appendix
I
(“eye”).
çj
UPon the reauest of the Aaencv, sam~1ingand
analysis of the hazardous waste
(and other
fuels
and
industrial
furnace
feed
stocks
as
aDpropriate) and the stack aas emissions must
be
conducted
to
verify
that
the
operating
conditions
established
in
the
certification
of precom~lianceor certification of
compliance achieve the applicable standards
of
Sections
726.204.
726.205,
726.206
and
726.207.
ii
The BIF and associated equipment (pumps, valves,
pipes, fuel storage tanks.
etc.) must be subiected
to thorouah visual inspection when they contain
hazardous waste.
at least daily for leaks. —spills,
fugitive emissions and signs of tampering.
fl
The automatic hazardous waste feed cutoff system
and
associated
alarms
must be tested at least once
every
7- days when hazardous waste is burned to
verify operability, unless the owner or operator
can demonstrate that weekly inspections will
unduly restrict or upset operations and that less
frequent inspections will be adequate.
Su~~ort
for such demonstration must be included in the
operating record.
At a minimum, operational
testing must be conducted at least once every 30
days.
~j
These monitoring and inspection data must be
recorded and the records must be placed in the
operating log.
~
Recordkeeping.
The owner or operator shall keep in the
operatina record of the facility all information and
data required by this Section until closure of the BIF
unit.
fl
Closure.
At closure, the owner or operator shall
remove all hazardous waste and hazardous waste residues
(including, but not limited to.
ash, scrubber waters
and scrubber sludges)
from the BIF and shall com~lv
with 35 Ill. Adm. Code 725.211
—
725.215.
(Source:
Added at 16 Ill.
Reg.
,
effective
)
128—707
238
Section
726.204
Standards
to
control
Organic
Emissions
~
DRE standard.
~
General.
Except
as
provided
in
subsection
(a)
(3),
a BIF burning hazardous waste must achieve a DRE
of 99.99
for all organic hazardous constituents
in the waste feed.
To demonstrate conformance
with this reguirement, 99,99
DRE must be
demonstrated during a trial burn for each
principal organic hazardous constituent
(POHC)
designated
(under subsection
(p1(2))
in its
permit
for each waste feed.
DRE is determined for each
P01-IC from the following equation:
DRE
= 100(1
—
0)/I
where:
I
=
Mass feed rate of one POHC in the hazardous
waste fired to the BIF;
and
O
=
Mass emission rate of the same POHC present in
stack gas prior to release to the atmosphere.
21
Designation of POHCs.
POHCs are those compounds
for which compliance with the DRE requirements of
this Section must be demonstrated in a trial burn
in conformance with procedures prescribed in 35
Ill. Adm. Code 703.232.
One or more POHCs must be
designated by the Agency for each waste feed to be
burned.
POHCS must be designated based on the
dearee of difficulty of destruction of the organic
constituents in the waste and on their
concentrations or mass in the waste feed
considering the results of waste analyses
submitted with Part B of the permit application.
POHCs are most likely to be selected from among
those compounds listed in 35
Ill.
Adm. Code
721.Appendix H that are also Present in the normal
waste feed.
However,
if the applicant
demonstrates to the A~encvthat a compound not
listed
in
35 Ill. Adm. Code 721.Appendix H or not
present in the normal waste feed is a suitable
indicator of compliance with the DRE requirements
of this Section. that compound must be designated
as a POHC.
Such POHCs need not be toxic or
organic compounds.
21
Dioxin-listed waste.
A BIF burning hazardous
waste containing
(or derived from)
USEPA Hazardous
Wastes Nos.
F020.
F021,
F022.
F023,
F026 or F027
128—708
239
must achieve a destruction and removal efficiency
(DREI of 99.9999
for each POHC designated
(under
subsection
(a)
(2))
in its permit.
This
performance must be demonstrated on ?OHCs that are
more difficult to burn than tetra-. penta- and
hexachlorodibenzo—p—dioxins
and
dibenzofurans.
DRE is determined for each
POHC
from
the
equation
in subsection
(a) (1).
In addition, the owner or
operator of the BIF shall notify the Aaency of
intent to burn USEPA Hazardous Waste Nos.
F020.
P021.
P022. P023.
P026 or F027.
j)
Automatic
waiver of DRE trial burn.
Owners and
operators
of
boilers
operated
under
the special
operating requirements provided by Section 726.210
are considered to be in compliance with the DRE
standard of subsection
(a) (1) and are exempt from
the DRE trial burn.
.~J..
Low risk waste.
Owners and operators of BIFs that
burn hazardous waste in compliance with the
requirements of Section 726.209(a)
are considered
to be in compliance with the DRE standard of
subsection
(a) (1) and are exempt from the DRE
trial burn.
CO standard.
ii
Except as provided in subsection
(c). the stack
gas concentration of CO
from a BIF burning
hazardous waste cannot exceed 100 ppmv on an
hourly rolling average basis
(i.e.,
over any 60
minute period). continuously corrected to
7
percent oxygen. dry gas basis.
21
CO and oxygen must be continuously monitored in
conformance with “Performance Specifications for
Continuous Emission Monitoring of Carbon Monoxide
and Oxygen for Incinerators. Boilers. and
Industrial Furnaces Burning Hazardous Waste” in
Appendix
I
(“eye”).
21
Compliance with the 100 ppmv CO limit must be
demonstrated during the trial burn
(for new
facilities or an interim status facility an~lving
for a permit) or the compliance test (for interim
status
facilities).
To
demonstrate
compliance.
the highest hourly rolling averaae CO level during
any valid run of the trial burn or compliance test
must not exceed 100 ppmv.
çj
Alternative CO standard.
128—709
240
~
The stack gas concentration of CO
from a BIF
burning hazardous waste may exceed the 100 ppinv
limit provided,that stack gas concentrations of
HCs
do not exceed 20 opmv. except as provided by
subsection
(f)
for certain industrial furnaces~
21
MC limits must be established under this Section
on an hourly rolling average basis
(i.e.. over any
60 minute period).
reported
as propane1 and
continuously corrected to 7 percent oxygen, dry
gas basis.
~J
MC must be continuously monitored in conformance
with “Performance Specifications for Continuous
Emission Monitoring of Hydrocarbons for
Incinerators, Boilers, and Industrial Furnaces
Burning Hazardous Waste” in Appendix
I
(“eye”).
CO and oxygen must be continuously monitored in
conformance with subsection
(b)(2).
il
The alternative CO standard is established based
on CO data during the trial burn
(for a new
facility) and the compliance test
(for an interim
status facility).
The alternative CO standard is
the average over all valid runs of the highest
hourly average CO level for each run.
The CO
limit is implemented on an hourly rolling average
basis.
and continuously corrected to 7 percent
oxygen, dry gas basis.
~j
Special requirements for furnaces.
Owners and
operators of industrial furnaces
(e.g.. kilns. cu~olas)
that feed hazardous waste for a purpose other than
solely as an ingredient (see Section 726.203(a) (5) (B))
at any location other than the end where products are
normally discharged and where fuels are normally fired
must comply with the MC limits provided by subsections
(c)
or
(f) irrespective of whether stack gas CO
concentrations meet the 100 p~mvlimit of subsection
(b).
~j
Controls for dioxins and furans.
Owners and operators
of
BIFs that are equipped with a dry PM control device
that operates within the temperature range of 450-750
°F,and industrial furnaces operating under an
alternative MC limit established under subsection
(f)
shall conduct a site—specific risk assessment as
foi.lows to demonstrate that emissions of chlorinated
dibenzo—p—dioxins and dibenzofurans do not result in an
increased lifetime cancer risk to the hypothetical
128—710
241
maximum exposed individual
(MEl) exceeding 1E-05
(1 in
100.000):
fl.
During the trial burn
(for new facilities or an
interim status facility a~~lvingfor a permit)
or
compliance test
(for interim status facilities),
determine emission rates of the tetra-octa
congeners of chlorinated dibenzo-p-dioxins
(PCDDs)
and dibenzofurans
(CDDs/CDFs) using Method 23.
“Determination of Po.ychlorinated
Dibenzo-p-
Dioxins and Polychiorinated Dibenzofurans
(PCDFs)
prom Stationary Sources”,
in Ammendix
I (“eye”)
21
Estimate the 2.3.7.8-TCDD toxicity equivalence of
the tetra—octa CDDs/CDFs congeners using
“Procedures for Estimating the Toxicity
Equivalence of Chlorinated Dibenzo-p-Dioxin and
Dibenzofuran Congeners” in Appendix
I
(“eye”).
Multiply the emission rates of CDD/CDF congeners
with a toxicity equivalence greater than zero (see
the procedure) by the calculated toxicity
equivalence factor to estimate the equivalent
emission rate of 2.3,7,8—TCDD
21
Conduct dispersion modeling using methods
recommended in “Guideline on Air Quality Models
(Revised)” or the “Hazardous Waste Combustion Air
quality Screening Procedure”, which are provided
in Appendices
I and .J, respectively, or “EPA
SCREEN Screening Procedure” as described in
Screening Procedures for Estimating Air Quality
Impact of Stationary Sources (incorporated by
reference in 35 Ill.
Adm. Code 720.111) to predict
the maximum annual average off—site ground level
concentration of 2.3.7.8—TCDD equivalents
determined under subsection
(e) (2).
The maximum
annual average on—site concentration must be used
when a person resides on—site;
and
Al
The ratio of the predicted maximum annual average
ground level concentration of 2,37.8-TCDD
equivalents to the risk-specific dose
(RSD)
for
2,3,7,8-TCDD provided in Appendix E
(2.2E-07) must
not exceed 10.
~j
Alternative MC limit for furnaces with organic matter
in raw material.
For industrial furnaces that cannot
meet the 20 ppmv MC limit because of organic matter in
normal raw material, the Agency shall establish an
alternative MC limit on a case—by—case basis
(under a
Part B permit proceeding)
at a level that ensures that
flue gas
IIC
(and CO) concentrations when burning
128—7 11
242
hazardous waste are not areater than when not burning
hazardous waste (the baseline MC level) provided that
the owner or operator complies with the following
requirements.
However,
cement kilns equipped with a
by-pass duct meeting the requirements of subsection
(gi. are not eligible for an alternative MC limit.
fl
The owner or operator shall demonstrate that the
facility is designed and operated to minimize MC
emissions from fuels and raw materials when the
baseline MC (and CO)
level
is determined.
The
baseline MC (and CO)
level
is defined as the
average over all valid test runs of the highest
hourly rolling average value for each run when the
facility does not burn hazardous waste, and
produces normal products under normal operating
conditions feeding normal feedstocks and fuels.
More than one baseline level must be determined if
the facility operates under different modes that
generate sianificantly different MC
(and CO)
levels
21
The owner or operator shall develop an approach to
monitor over time changes in the operation of the
facility that could reduce the baseline MC level
21
The owner or operator shall conduct emissions
testing during the trial burn to:
~j
Determine the baseline MC
(and CO)
level
p1
Demonstrate that, when hazardous waste is
burned, MC (and CO) levels do not exceed the
baseline level;
and
çj
Identify the types and concentrations of
organic compounds listed in 35 Ill. Adm. Code
721.Appendjx H. that are emitted and conduct
dispersion modelin~to predict the maximum
annual average around level concentration of
each oraan.jc compound.
On—site around level
concentrations must be considered for this
evaluation if a person resides on site.
jj.
Sampling and analysis of organic
emissions must .be conducted using
procedures prescribed by the Agency
pursuant to 35 Ill. Adm. Code
703.208(a).
128—712
243
£iI
Dispersion modeling must be conducted
according to procedures provided by
subsection
(e) (2);
and
~j
Demonstrate that maximum annual average
around level concentrations of the organic
compounds identified in subsection
(f) (3) (C)
do not exceed the following levels:
LL
For the noncarcinogenic compounds listed
in Appendix D. the levels established in
Appendix D
jjJ
For the carcinogenic compounds listed in
Appendix E, the sum for all compounds of
the ratios of the actual ground level.
concentration to the level established
in Appendix E cannot exceed
1.0.
To
estimate the health risk from
chlorinated dibenzo-p—dioxins and
dibenzofuran congeners. use the
procedures prescribed by subsection
(e)(3)
to estimate the 2.3,7,8—TCDD
toxicity equivalence of the congeners.
iii) For compounds not listed in Appendix D
or E.
0.1 uq/cu
in.
Al
All MC levels specified under this subsection are
to be monitored and reported as specified in
subsections
(c) (1) and
(2).
gj
Monitoring CO and MC in .the by-pass duct of a cement
kiln.
Cement kilns may comply with the CO and MC
limits provided by subsections
(bY,
(c) and
(d) by
monitoring in the by-pass duct provided that:
fl
Hazardous waste is fired only into the kiln and
not at any location downstream from the kiln exit
relative to the direction of gas flow;
and
21
The by-pass duct diverts a minimum of 10
of kiln
off-gas into the duct.
j~j
Use of emissions test data to demonstrate compliance
and establish operating limits.
Compliance with the
requirements of this Section must be demonstrated
simultaneously by emissions testing or during separate
runs under identical operating conditions.
Further,
data to demonstrate compliance with the CO and MC
limits of this Section or to establish alternative CO
or MC limits under this Section must be obtained during
128—713
244
the time that DRE testina.
and where applicable,
CDD/CDF testing under subsection
(e) and comprehensive
organic emissions testing under subsection
(f)
is
conducted.
Jj
Enforcement.
For the purposes of permit enforcement.
compliance with the operating requirements specified in
the permit (under Section 726.202) will be reaarded as
compliance with this Section.
However, evidence that
compliance with those permit conditions
is insufficient
to ensure compliance with the requirements of this
Section is “information” tustifving modification or
revocation and re-issuance of a permit under 35 Ill.
Adm. Code 703.270 et sea.
(Source:
Aded at 16 Ill. Reg.
,
effective
)
Section 726.205
Standards to control PM
~j.
A BIF burning hazardous waste must not emit PM in
excess of 180 ma/dry standard cu a
(0.08 grains/dry
standard cubic foot)
after correction to a stack gas
concentration of 7
oxygen. using Procedures prescribed
in 40 CFR
60..., Appendix A. methods
3. through
5
(incorporated by reference in 35
Ill.
Ada. Code
720.111)~,and APpendix I
(“eye”).
~j
An owner or operator meeting the requirements of
Section 726.209(b)
for the low risk waste sxemption is
exemPt from the PM standard.
~j
For the Purposes of permit enforcement, compliance with
the operating requirements specified in the permit
(under Section 726.202) will be regarded as compliance
with this Section.
However, evidence that compliance
with those permit conditions is insufficient to ensure
compliance with the requirements of this Section is
“information” ~ustifyina modification or revocation and
re—issuance of a permit under 35 Ill.
Adm
Code 703.270
et seq.
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section 726.206
Standards to control Metals Emissions
~j
General.
The owner or operator shall comply with the
netals standards .provided by subsections
(b),
Cc).
Cd),
~e) or
(f)
for each metal listed in subsection
(b) that
is present in the hazardous waste at detectable levels
using analytical procedures specified in Test Methods
128—7
14
245
for Evaluating Solid Waste. Physical/Chemical Methods
(SW-846). incorporated by reference in 35
Ill. Ada.
Code 720.111.
~
Tier
I feed rate screening limits.
Feed rate screening
limits for metals are specified in Appendix A as a
function of terrain-adiusted effective stack height
(TESH)
and terrain and land use in the vicinity of the
facility.
Criteria for facilities that are not
eligible to comply with the screening limits are
provided in subsection
(b) (7).
~j
Noncarcinogenic metals.
The feed rates of the
noncarcinogenic metals in all feed streams.
including hazardous waste,
fuels and industrial
furnace feed stocks must not exceed the screening
limits specified in Appendix A.
~j.. The feed rate screening limits for antimony.
barium, mercury. thallium and silver are
based on either:
il
An hourly rolling average as defined in
Sections 726.200(g)
and
726.202(e) (6) (A) (ii);
or
JJJ
An instantaneous limit not to be
exceeded at any time.
p1
The feed rate screening limit for lead is
based on one of the following:
j~
An hourly rolling average as defined in
Sections 726.200(g)
and
726.202(e) (6) (A) (ii)
ii1.
An averaging period of
2 to 24 hours as
defined in Section 726.202(e) (6) (B) with
an instantaneous feed rate limit not to
exceed 10 times the feed rate that would
be allowed on an hourly rolling average
basis;
or
iii)
An instantaneous limit not to be
exceeded at any time.
21
Carcinogenic metals.
~
The feed rates of carcinogenic metals in all
feed streams, including hazardous waste.
fuels and industrial furnace feed stocks must
not exceed values derived from the screening
128—7 15
246
limits specified in Appendix A.
The feed
rate of each of these metals is limited to a
level such that the sum of the ratios of the
actual
feed rate to the feed, rate screening
limit specified in Appendix A must not exceed
1.0. as provided by the following equation:
SUM(Ai/Fi)
1.0
where:
SUM(Xi)
means the
sum
of the values of X for
each metal
“i”.
from
I
=
1 to a.
n
=
number of carcinogenic metals
Ai
=
actual feed rate to the device for metal
I,
Fi
=
feed rate screening limit provided by
Appendix A for metal “i”.
p1
The feed rate screening limits for the
carcinogenic metals are based on either:
j)
An hourly rolling average;
or
~jJJ.
An averaging period of
2 to 24 hours,
as
defined in Section 726.202(e) (6) (B).
with an instantaneous feed rate limit
not to exceed
10 times the feed rate
that would be allowed on an hourly
rolling average basis.
TESH
(terrain adiusted effective stack height).
~
The TESH is determined according to the
following equation:
TESH=H+P-T
where:
H
=
Actual physical stack height
(m)
P
=
Plume rise
(in a)
as determined from
Appendix F as a function of stack flow rate
and stack gas exhaust temperature.
T
=
Terrain rise
(in a) within five
kilometers of the stack.
128—716
247
p1
The stack height
(H) must not exceed good
engineering
practice
stack
height.
as
defined
in Section 726.200(g).
~
if the TESH calculated pursuant to subsection
(bU3)(A)
is not listed in Appendices A
-
C.
the
values
for
the
nearest
lower
TESH
listed
in the table must be used.
If the TESH is
four meters or less,
a value based on four
meters must be used.
Al
Terrain type.
The screening limits are a function
of whether the facility is located in noncom~lex
or comDlex terrain.
A device located where any
part of the surrounding terrain within
5
kilometers of the stack eanals or exceeds the
elevation
of the physical stack height
(H)
is
considered
to
be
in
complex
terrain
and
the
screening
limits
for
complex
terrain
apply.
Terrain
measurements
are
to
be
made
from
U.S.
Geoloaical
Survey
7.5—minute
to~oaraphic
maPs
of
the
area
surroundina
the
facility.
~j
Land use.
The screening limits are a function of
whether~the facility is located in an area where
the land use is urban or rural.
To determine
whether land use in the vicinity of the facility
is
urban
or
rural.
procedures
provided
j~
Appendices
I
(“eye”).
or
J
shall
be
used.
~j
Multiple stacks.
Owners and oPerators of
facilities with more than one on—site stack from a
BIF.
incinerator or other thermal treatment unit
subiect
to
controls
of
metals
emissions
under
a
RCRA
permit or interim status controls shall
comPly with the screening limits for all such
units assuming
all
hazardous
waste
is
fed
into
the
device_with
the
worst—case
stack
based
on
dispersion
characteristics.
The
stack
with
the
lowest
value
of
K
is
the
worst—case
stack.
K
is
determined from the following equation as applied
to
each
stack:
K
=
H*V*T
Where:
K
=
a
Parameter
accounting
for
relative
influence
of stack height and Plume rise;
H
=
physical stack height (meters)
128—717
248
V
=
stack gas flow rate
(cu inlsecond);
and
T
=
exhaust
temperature
(dearees
K).
fl.
Criteria for facilities not eligible for screening
limits.
If any criteria below are met, the Tier I
(and Tier II) screening limits do not apply.
Owners and operators of such facilities shall
comply with the Tier III standards provided by
subsection
Cd).
~j
The device is located in a narrow valley less
than one kilometer wide
p1
The device has a stack taller than 20 meters
and is located such that the terrain rises to
the physical height within one kilometer of
the facility
Qj
The device has a stack taller than 20 meters
and is located within five kilometers of a
shoreline of a large body of water such as an
ocean or large lake
~j
The physical stack height of any stack is
less than 2.5 times .the height of any
building within five building heights or five
~ro~ected building widths of the stack and
the distance from the stack to the closest
boundary is within five building heights or
five projected building widths of the
associated building;
or
~J
The Agency determines that standards based on
site-specific dispersion modeling are
required.
p1
Implementation.
The feed rate of metals in each
feedstream must be monitored to ensure that the
feed rate screening limits are not exceeded.
~j
Tier II emission rate screening limits.
Emission rate
screening limits are specified in
Appendix
A
as
a
function of TESH and terrain and land use in the
vicinity of the facility.
Criteria for facilities that
are not eligible to comply with the screening limits
are provided in subsection
(b)(7).
~j
Noncarcinogenic metals.
The emission rates of
noncarcinogenic metals must not exceed the
screening limits specified in Appendix A.
1280718
249
21
Carcinogenic metals.
The emission rates of
carcinogenic metals must not exceed values derived
from the screening limits specified in Appendix A.
The emission rate of each of these metals is
limited to a level such that the sum
of
the
ratios
of the actual emission rate to the emission rate
screenina limit specified in Appendix A must not
exceed
1.0. as provided by the following
equation:
SUM(Ai/Ei) ?
1.0
where:
SUM(Xi) means the sum of
the
values
of
X for each
metal
i, from 1
=
1
to n.
n
=
number of carcinogenic metals
Ai
=
actual emission rate for metal “i”
Ei
=
emission rate screening limit provided by
Appendix A for metal “i”.
21
Implementation,
The emission rate limits must be
implemented by limiting feed rates of the
individual metals to levels during the trial burn
(for new facilities or an interim status facility
aPPlying for a permit) or the compliance test
(for
interim status facilities).
The feed rate
averaging periods are the same as .provided by
subsections
(b) (I) (A) and
(8) and
(b) (2) (B).
The
feed rate of metals in each feedstream must be
monitored to ensure. that the feed rate limits for
the feedstreams specified under Sections 726.202
or 726.203 are not exceeded.
Al
Definitions and limitations.
The definitions and
limitations provided bY subsection
(b) and
726.200(a). for the following terms also apply to
the Tier II emission rate screening limits
provided by subsection
(C):
TESH. aood
engineering practice stack height, terrain type.
land use and criteria for facilities not eligible
to use the screening limits.
~
Multiple stacks.
~j
Owners and operators of facilities with more
than one on-site stack from a BIF.
incinerator or other thermal treatment unit
subiect to controls on metals emissions under
a RCRA permit or interim status controls
128—719
250
shall comply with the emissions screening
limits for any such stacks assuming all
hazardous waste is fed into the device with
the worst—case stack based on dispersion
characteristics.
p1
The worst-case stack is determined by
procedures
provided
in
subsection
(b) (6).
çj
For each metal,
the
total
emissions of the
metal from those stacks must not exceed the
screening limit for the worst—case stack.
Tier III site—specific risk assessment.
~
General.
Conformance with the Tier 111 metals
controls must be demonstrated by emissions testing
to determine the emission rate for each metal. air
dispersion modeling to predict the maximum annual
average off—site around level concentration for
each metal and a demonstration that acceptable
ambient levels are not exceeded.
21
Acceptable ambient levels.
Appendices D and E
list the acceptable ambient levels for purposes of
this Subpart.
Reference air concentrations
(RACs)
are listed for the noncarcinogenic metals and 1E—
05 RSDs are listed for the carcinogenic metals.
The RSD for a metal
is the acceptable ambient
level for that metal provided that only one of the
four carcinogenic metals is emitted.
If more than
one carcinogenic metal is emitted, the acceptable
ambient level for the carcinogenic metals is a
fraction of the RSD as described in subsection
(d) (3)
21
Carcinogenic metals.
For the carcinogenic metals
the sum of the ratios
of the predicted maximum
annual
average off-site ground level
concentrations (except that on—site concentrations
must be considered if a person resides on site) to
the RSD for all carcinoaenic metals emitted must
not exceed 1.0 as determined by the following
equation:
SUM(Pi/Ri) ?
1.0
where:
SUM(Xi)
means the sum of the values of X for each
metal i, from
i
=
1 to n.
128—7 20
251
n
=
number of carcinogenic metals
Pi
=
Predicted
ambient
concentration
for
metal
i.
Ri
=
RSD for metal
i.
41
Noncarcinogenic
metals,
For
the
noncarcinogenic
metals,
the
predicted
maximum
annual
average
off-
site around level concentration for each metal
must not exceed the RAC.
~j.
Multiple
stacks.
Owners
and
operators
of
facilities with more than one on—site stack from a
BIF.
incinerator
or
other
thermal
treatment
unit
sub-ject to controls on metals emissions under a
RCRA_permit or interim status controls shall
conduct emissions testing and dispersion modeling
to demonstrate that the aaareaate emissions from
all such On—site stacks do not result in an
exceedance of the acceptable ambient levels.
~j
Implementation.
Under Tier III. the metals
controls must be implemented by limiting feed
rates of the individual metals to levels during
the trial burn
(for new facilities or an interim
status facility applyina for a
permit)
or the
compliance test
(for interim status facilities).
The feed rate averaging periods are the same as
provided by subsections
(b) (1) (A) and
(B) and
(b) (2) (B)
•
The feed rate of metals in each
feedstreain must be monitored to ensure that the
feed rate limits for the feedstreaius specified
under Sections 726.202 or 726.203 are not
exceeded.
,~j
Adjusted Tier I feed rate screening limits.
The owner
or operator may adjust the feed rate screening limits
provided by Appendix A to account for site-specific
dispersion modeling.
Under this approach, the adjusted
feed rate screening limit for a metal is determined by
back—calculating from the acceptable ambient levels
provided by Appendices D and E using dispersion
modeling to determine the maximum allowable emission
rate.
This emission rate becomes th~adiusted Tier
I
feed rate screening limit.
The feed rate screening
limits for carcinogenic metals are
implemented
as
prescribed
in
subsection
(b) (2).
fj
Alternative implementation approaches.
j).
Pursuant to subsection
(f) (2). the Aaency shall
approve on a case-by—case basis approaches to
128—721
252
implement the Tier II or Tier III metals emission
limits provided by subsections
(c) or
(d)
alternative to monitoring the feed rate of metals
in each feedstream.
21
The emission limits provided by subsection
(di
must be determined as follows:
~j
For each noncarcinogenic metal.
by back—
calculating from the RAC provided in
Appendix
D to determine the allowable emission rate
for each metal using the dilution factor for
the maximum annual average around level
concentration predicted by dispersion
modeling in conformance with subsection
(hi;
and
p1
For each carcinogenic metal by:
Jj
Back-calculating from the RSD provided
in
Appendix
E
to determine ~theallowable
emission rate for each metal if.that
metal were the only carcinogenic metal
emitted using the dilution factor for
the maximum annual average ground level
concentration predicted by dispersion
modeling in conformance with subsection
(h):
and
.111
If more than one carcinogenic metal
is
emitted, selecting an emission limit for
each carcinogenic metal not to exceed
the emission rate determined by
subsection
(f) (2) (B) (i)
such that the
sum for all carcinogenic metals of the
ratios of the selected emission limit to
the emission rate determined by that
subsection does not exceed 1.0.
g.
Emission testing.
3j
General.
Emission testing for metals must be
conducted using the Multiple Metals Train as
described in Appendix I
(“eye”).
21
Hexavalent chromium.
Emissions of chromium are
assumed to be hexavalent chromium unless the owner
or operator conducts emissions testing to
determine hexavalent chromium emissions using
procedures prescribed in Appendix
I
(“eye”).
128—722
253
j~j
Dispersion modeling.
Dispersion modeling reauired
under this Section must be conducted according to
methods recommended in Appendix J. the “Hazardous Waste
Combustion Air Quality Screening Procedure” described
in Appendix I (“eye”). or
“EPA
SCREEN
Screening
Procedure” as described in Screening Procedures for
Estimating
Air
Quality
Impact
of
Stationary
Sources
(the latter document is incor~oratedby reference.
see
35 Ill.
Adm. Code
720.111)
to
predict
the
maximum
annual
average
off-site
around
level
concentration.
However, on—site concentrations must be considered when
a
person
resides
on—site..
j)
Enforcement.
For the purposes of permit enforcement,
compliance with the operating requirements specified in
the permit
(under Section 726.202) will be regarded as
compliance with this Section.
However, evidence that
compliance with those permit conditions is insufficient
to ensure compliance with the requirements of this
Section is “information” justifvina modification or
revocation and re—issuance of a permit under 35 Ill.
Adm.
Code 703.270 et seq.
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section 726.207
Standards to Control HC1 and Chlorine Gas
Emissions
~j
General.
The owner or operator shall comply with the
HC1 and chlorine gas controls provided by subsections
(b)
or
(c).
~
Screening limits.
~j
Tier I feed rate screening limits.
Feed rate
screening limits are specified for total chlorine
in_Appendix B as a function of TESH and terrain
and land use in the vicinity of the facility.
The
feed
rate
of
total
chlorine
and
chloride,
both
organic and inorganic,
in all feed streams,
including hazardous waste. fuels and industrial
furnace feed stocks must not eçceed the levels
specified.
21
Tier II emission rate screening limits.
Emission
rate screening limits for HCl and chlorine gas are
specified in Appendix C as a function of TESH and
terrain and land use in the vicinity of the
facility.
The stack emission rates of HC1 and
chlorine gas must not exceed the levels specified.
128—7
23
254
j~
Definitions and limitations.
The definitions and
limitations provided by Section 726.200(g)
and
726.206(b)
for the following terms also apply to
the screening limits provided by this subsection:
TESH.
good engineering practice. stack height,
terrain
type.
land use and criteria for facilities
not eligible to use the screening limits.
j)
Multiple stacks.
Owners
and operators of
facilities with more than one on—site stack from
a
BIF.
incinerator or other
thermal
treatment unit
subject to controls on Md
or chlorine gas
emissions under a RCRA permit or interim status
controls shall com~lvwith the Tier
I and Tier II
screenina limits for those stacks assuming all
hazardous waste
is fed into the device with the
worst—case stack based on dispersion
characteristics.
~j.
The worst-case stack is determined by
procedures provided in Section 726.206(b) (6).
p1
Under Tier I. the total feed rate of chlorine
and chloride to all subiect devices must not
exceed
the screening limit for the worst—case
stack.
~Q1.
Under Tier II. the total emissions of MCi and
chlorine gas from all subiect stacks must not
exceed the screening limit for the worst—case
stack.
~J
Tier III site—specific risk assessments.
~
General.
Conformance with the Tier III controls
must be demonstrated by emissions testing to
determine the emission rate for HC1 and chlorine
gas, air dispersion modeling to predict the
maximum annual average off—site around level
concentration for each compound, and a
demonstration that acceptable ambient levels are
not exceeded.
21
Acceptable
ambient
levels.
Appendix
ID lists the
RACs
for MCi
(7 ua/cu ml and chlorine gas
(0.4
ug/cu
a)
~J.
Multiple stacks.
Owners and operators of
facilities with more than one on-site stack from a
BIF. incinerator or other thermal treatment unit
subject to controls on HC1 or chlorine gas
e~rissionsunder a RCRA permit or interim status
128—7
24
255
controls shall conduct emissions testing and
dispersion modeling to demonstrate that the
aaareaate emissions from all such on-site stacks
do not result in an exceedance of theacceptable
ambient levels for MCi and chlorine gas.
~j
Averaging periods.
The MCi and chlorine gas controls
are implemented by limiting the feed rate of total
chlorine and chloride in all feedstreams. including
hazardous waste, fuels and industrial furnace feed
stocks.
Under Tier I. the feed rate of total chlorine
and chloride is limited to the Tier I Screening Limits.
Under Tier II and Tier III. the feed rate of total
chlorine and chloride is limited to the feed rates
during the trial burn (for new facilities or an interim
status facility applying for a permit)
or the
compliance test
(for interim status facilities).
The
feed rate limits are based on either:
fl..
An hourly rolling average as defined-in Section
726.200(g)
and 726.2.02(e)(6);
or
21
An instantaneous basis not to be exceeded at any
time.
~j
Adiusted Tier I feed rate screening limits.
The owni
or operator may adiust the feed rate screening limit
provided by Appendix B to account for site-specific
dispersion modeling.
Under this approach. the adjusted
feed rate screening limit
is determined by back-
calculating from the acceptable ambient level for
chlorine gas provided by Appendix D using dispersion
modeling to determine the maximum allowable emission
rate.
This emission rate becomes the adjusted Tier
I
feed rate screening limit.
fj.
Emiss ons testing.
Emissions testing for MCi and
chlorine
gas
must
be
conducted
using
the
procedures
described in Appendix
I
(“eye”).
gi
Dispersion
modeling.
Dispersion
modeling
must
be
conducted
according
to
the
provisions
of
Section
726.206(h)’.
~j
Enforcement.
For
the
purposes
of
permit
enforcement,
compliance
with
the
operatina
requirements
specified
in
the permit
(under Section 726.2021 will be regarded as
compliance
with
this
Section.
However,
evidence
that
compliance
with
those
permit
conditions
is
insufficient
to
ensure
compliance
with
the
requirements
of
this
Section is “information” iustifyina modification or
128—725
256
revocation and re—issuance of a permit under 35 Ill.
Ada. Code 703.270 et sea.
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section 726~208 Small quantity On-site Burner Exemption
~j.. Exempt quantities.
Owners
and
operators
of
facilities
that
burn
hazardous
waste
in
an
on-site
BIF
are
exempt
from_the requirements of this Subpart provided that:
flU.
The
quantity
of
hazardous
waste
burned
in
a
device
for_a_calendar
month
does
not
exceed
the
limits
provided in the Table A based on the TESH as
defined in Section 726.200(a) and 726.206(b) (3).
21
The maximum hazardous waste firing rate does not
exceed at any time
1 percent of the total fuel
requirements for the device
(hazardous waste Plus
other fuel)
on a total heat input or mass input
basis, whichever results in the lower mass feed
rate of hazardous waste:
21
The hazardous waste has a minimum heating value of
5,000 Btu/lb. as generated;
and
4j
The hazardous waste fuel does not contain
(and is
not
derived
from)
tJSEPA
Hazardous
Waste
Nos.
F020,
F021. F022.
F023.
F026 or F027.
~
Mixing with nonhazardous fuels.
If hazardous waste
fuel
is
mixed
with
a
nonhazardous
fuel.
the
auantity
of
hazardous waste before such mixing is used to comply
with subsection
(a).
gi
Multiple stacks.
If an owner or operator burns
hazardous waste in more than one on—site BIF exempt
under this Section. the quantity limits provided by
subsection
(a) (1) are implemented according to the
following equation:
SUM(Ci/Li) ?
1.0
where:
SUM(Xi) means the sum of the values of X for each stack
i, from
i
=
1
to n
n means the number of stacks
128—726
257
Ci
=
Actual
Quantity
Burned means the waste auantity
burned
per month in device “i”.
Li
=
Allowable
Quantity
Burned
means
the
maximum
allowable exempt quantity for stack “i” from Table A.
BOARD NOTE:
Hazardous wastes that are subject to the
special
requirements
for
small
quantity
generators
under
35
Ill.
Ada. Code
721.105
may
be
burned
in
an
off-site device under the exemption provided by Section
726.208. but must be included in the quantity
determination for the exemption.
~j
Notification reauirements.
The owner or operator of
facilities qualifying for the small quantity burner
exemption under this Section shall provide a one—time
sianed, written notice to the Agency indicating the
following:
fi..
The combustion unit is operating as a small
quantity burner
of
hazardous
waste
~J..
The owner and operator are in compliance with the
requirements of this Section;
and
IL
The maximum auantity of hazardous waste that the
facility is allowed to burn per month as provided
by Section 726.208(a) (1).
gi
Recordkeeping requirements.
The owner or operator
shall maintain at the facility for at least three years
sufficient records documenting compliance with the
hazardous waste quantity. firing rate and heating value
limits of this Section.
At a minimum, these records
must indicate the quantity of hazardous waste and other
fuel burned in each unit ~er calendar month and the
heating value of the hazardous waste.
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section 726.209
Low risk waste Exemption
~j
Waiver
of
DRE
standard.
The
DRE
standard
of
Section
726.204(a) does not a~~lyif the BIF is operated in
conformance with subsection
(a) (1) and the owner or
operator demonstrates bY
procedures
prescribed
in
subsection
(a) (2)
that the burning will not result in
unacceptable adverse health effects.
fl.
The device must be operated as follows:
128—727
258
~
A
minimum
of
50
percent
of fuel fired to the
device must be fossil fuel,
fuels derived
from fossil fuel, tall oil or,
if approved by
the
Agency
on
a
case—by-case
basis,
other
nonhazardous
fuel
with
combustion
characteristics
com~arab1e to
fossil
fuel.
Such
fuels
are
termed
“primary
fuel”
for
purposes of this Section.
(Tall oil is a
fuel derived from veaetable and rosin fatty
acids.)
The
50
PerCent
primary
fuel
firing
rate
must
be
determined
on
a
total
heat
or
mass input basis. whichever results in the
greater
mass
feed
rate
of
Primary
fuel
fired
p1
Primary fuels and hazardous waste fuels must
have a minimum as—fired heating value of
8.000 Btu/lb
~
The hazardous waste is fired directly into
the primary fuel flame zone of the combustion
chamber;
and
Qj
The
device
operates
in
conformance
with
the
CO controls provided by Section
72G.204(b)(1).
Devices
subiect
to
the
exemption
provided
by
this
Section
are
not
eligible
for
the
alternative
CO
controls
provided by Section 726.204(c).
21
Procedures to demonstrate that the hazardous waste
burning will not pose unacceptable adverse public
health effects are as follows:
~
Identify and auantify those nonmetal
compounds listed in 35 Ill. Adm. Code
721.A~pendix
H. that could reasonably be
expected
to
be
present
in
the
hazardous
waste.
The constituents excluded from
analysis must be identified and the basis for
their
exclusion
explained
p1
Calculate
reasonable,
worst
case
emission
rates for each constituent identified in
subsection
(a)
(2)
(Al
by
assuming
the
device
achieves
99.9
percent
destruction
and
removal
efficiency.
That is, assume that 0.1 percent
of
the
mass
weiaht
of
each
constituent
fed
to
the
device
is
emitted.
Qj
For each constituent identified in subsection
(a) (2) (A). use emissions dispersion modeling
128—728
259
to
predict
the
maximum
annual
average
around
level
concentration
of
the
constituent.
j)
Dispersion
modeling
must be conducted
using
methods
specified
in
Section
726.206(h).
jjJ.
Owners
and
operators
pf
facilities
with
more
than
one
on—site
stack
from
a
BIF
that is exempt under this Section shall
conduct
dispersion
modeling
of
emissions
from
all
stacks
exempt
under
this
Section
to
predict
ambient
levels
prescribed
by
this
subsection.
Qj
Ground
level
concentrations
of
constituents
predicted under subsection
(a) (2) (C) must not
exceed
the
following
levels:
j)
For the noncarcinocienic compounds listed
in Appendix D.
the levels established in
Appendix D
jJJ
For the carcinogenic compounds listed in
Appendix E. thesum for all constituents
of the ratios of the actual ground level
concentration to the level established
in
Appendix
E
cannot
exceed
1.0;
and
iii)
For constituents not listed in Appendix
D or E.
0.1 ua/cu m.
~
Waiver of particular matter standard.
The PM standard
of Section 726.205 does not apply if:
fl
The DRE standard is waived under subsection (a)
and
21
The owner or operator complies with the Tier I.
or
adjusted Tier I. metals feed rate screening limits
provided
by
Section
726.206(b)
or
(e).
(Source:
Added at 16 Iii.
Reg.
,
effective
Section 726.210
Waiver of DRE trial burn for Boilers
Boilers that operate under the special requirements of this
Section, and that do not burn hazardous waste containing
(or
derived from)
USEPA Hazardous Waste Nos.
F020,
F021,
F022.
F023.
F026 or F027, are considered to be in conformance with the DRE
128—729
260
standard
of
Section
726.204(a).
and
a
trial
burn
to
demonstrate
DRE
is waived.
When burning hazardous waste:
~j
A
minimum
of
50
percent
of
fuel
fired
to
the
devices
must
be
fossil
fuel,
fuels
derived
from
fossil
fuel,
tall
oil
or,
if
approved
by
the
Aaencv
on
a
case-by-
case basis, other nonhazardous fuel with combustion
characteristics comparable to fossil fuel.
Such fuels
are
termed
“primary
fuel”
for
purposes
of
this
Section.
(Tall oil is a fuel derived from vegetable and rosin
fatty acids.) The 50 percent primary fuel firing rate
must be determined on a total heat or mass input basis,
whichever results in the greater mass feed rate of
primary fuel fired
~j
Boiler load must not be less than 40 percent.
Boiler
load is the ratio at any time of the total heat input
to the maximum design heat input:
çj
Primary fuels and hazardous waste fuels must have a
minimum as-fired heating value of 8,000 Btu/lb. and
each material fired in a burner where hazardous waste
is fired must have a heating value of at least 8,000
Btu/lb. as—fired
~
The device must operate in conformance with the CO
standard provided by Section 726.204(b) (1).
Boilers
subject to the waiver of the DRE trial burn provided by
this Section are not eligible for the alternative CO
standard provided by Section 726.204(c)
gi
The boiler must be a water tube type boiler that does
not feed fuel using a stoker or stoker type mechanism
and
fl
The hazardous waste must be fired directly into the
primary fuel flame zone of the combustion chamber with
an air or steam atomization firing system. mechanical
atomization system or a rotary cu~atomization system
under the following conditions:
fl.
Viscosity.
The viscosity of the hazardous waste
fuel as—fired must not exceed 300 SSU
21
Particle size.
When a
high
pressure
air
or
steam
atomizer,
low
pressure
atomizer
or
mechanical
atomizer
is
used.
70
of
the
hazardous
waste
fuel
must pass through a 200 mesh
(74 micron)
screen.
and when a rotary cup
atomizer
is used,
70
of the
hazardous waste must pass through a 100 mesh (150
micron) screen
128—730
261
IL
Mechanical atomization systems.
Fuel Pressure
within a
mechanical
atomization
system and fuel
flow rate must be maintained within the design
ranae
taking
into
account
the
viscosity
and
volatility
of
the
fuel
il
RotarY
cup
atomization
systems.
Fuel flow rate
through
a
rotary
cu~ atomization
system
must
be
maintained
within
the
design
ranae
taking
into
account the viscosity and volatility of the fuel.
(Source:
Added
at
16
Ill.
Reg.
,
effective
)
Section 726.211
Standards for direct Transfer
~j
Applicability.
The regulations
in this Section a~~lv
to
owners
and
operators
of
BIFs
subject
to
Sections
726.202 or 726.203
if hazardous waste is directly
transferred from a transport vehicle to a BIF wtthout
the use of a storage unit.
Definitions.
fl
When
used
in
this
Section.
the
following
terms
have the meanings given below:
Direct transfer equipment means any device
(including but not limited to, such devices
as pipina. fittings. flanges, valves and
pumps) that is used to distribute. meter or
control the flow of hazardous waste between a
container (i.e., transport vehicle) and a
BIF.
Container means any portable device in which
hazardous waste is
transported,
stored.
treated or otherwise handled. and includes
transport
vehicles
that
are
containers
themselves
(e.g.,
tank trucks, tanker—
trailers
and
rail
tank
cars)
and
containers
placed
on
or
in
a
transport
vehicle.
21
This Section
references
several
requirements
provided
in
35
Ill.
Ada.
Code
724
and
725.Subparts
I
and
J.
For
purposes
of
this
Section.
the
term
“tank systems” in those referenced requirements
means direct transfer equipment as defined in
subsection
(b) (1).
~n~ra1
ôn~r~tinarequir~m~nt~-
128—731
262
fl
No direct transfer of a ~um~able hazardous waste
must be conducted from an open—top container to a
BIF.
21
Direct
transfer
equipment
used
for
pumpable
hazardous
waste
must
always
be
closed,
except
whefl
necessary
to
add
or
remove
the
waste,
and
must
not
be
opened.
handled
or
stored
in
a
manner
that
could cause any rupture or leak.
IL
The direct transfer of hazardous waste to a BIF
must_be conducted so that it does not:
~j
Generate extreme heat or pressure,
fire,
explosion or violent reaction
p1
Produce uncontrolled toxic mists,
fumes,
dusts or gases
in sufficient quantities to
threaten human health
~
Produce uncontrolled flammable fumes or gases
in sufficient guantities to pose a risk of
fire or explosions
Qj
Damage the structural integrity of the
container or direct transfer eguipment
containing the waste
p1
Adversely affect the capability of the BIF to
meet the standards provided by Sections
726.204 through 726.207;
or
p1
Threaten human health or the environment.
4j
Hazardous waste must not be placed in direct
transfer equipment,
if it could cause the
equipment or its secondary containment system to
rupture.
leak.
corrode or otherwise fail.
~j
The
owner
or
operator
of
the
facility
shall
use
appropriate controls and practices to prevent
spills and overflows from the direct transfer
equipment or its secondary containment systems.
These include at
a minimum:
~j
Spill prevention controls (e.g..
check
valves,
dry
discount
couplings);
and
p1
Automatic waste feed cutoff to use if a leak
or spill occurs from the direct transfer
equipment.
128—7 32
263
~J
Areas where
direct
transfer
vehicles
(containers)
are
located.
A~~1ying
the
definition
of
container
under
this Section. owners and operators shall comply with
the following requirements:
fl
The containment requirements of 35 Ill. Adm.
Code
724.275
21
The
use
and
manaaement
reauirements
of
35
Ill.
Ada.
Code
725.Subpart
I,.
except
for
Sections
725.270 and 725.274, and except that in lieu of
the
special
requirements
of
35
Ill.
Ada.
Code
725.276
for
ignitable
or
reactive
waste,
the
owner
or operator may com~lvwith the requirements for
the
maintenance
of
protective
distances
between
the waste management area and any public ways.
streets,
alleys
or
an
adjacent
~ro~ertv
line
that
can
be
built
upon
as
required
in
Tables
2-1
through 2-6 of NFPA 30 (incorporated by reference
in
35
Ill.
Ada.
Code
720.111).
The
owner
or
operator
shall
obtain
and
keeP
on
file
at
the
facility a written certification by the local Fire
Marshal
that
the
installation
meets
the
subject
NFPA Codes;
and
IL
The closure requirements of 35 Ill. Ada. Code
724.278.
gi
Direct transfer eauipment.
Direct transfer equipment
must meet the following requirements:
fl
Secondary containment.
Owners and operators shall
com~lvwith the secondary containment requirements
of 35 Ill. Ada. Code 725.293
,
except
for
subsections 725.293(a),
(d).
(e) and
(i)
as
follows:
~j
For all new direct transfer equipment. prior
to their being put into service;
and
p1
For
existing
direct
transfer
equipment.
by
Auaust 21,
1993.
21
Requirements
prior
to
meeting
secondary
containment requirements.
~j
For
existing
direct
transfer
equipment
that
does
not
have
secondary
containment,
the
owner
or
operator
shall
determine
whether
the
equipment is leaking or is unfit for use.
The
owner
or
operator
shall
obtain
and
keen
on file at the facility
a written assessment
128—733
264
reviewed and certified by
p
qualified,
registered professional engineer in
accordance with 35 Ill.
Ada. Code 703.126td)
that attests to the equipment’s integrity by
Auaust 21.
1992.
p1
This assessment must determine whether the
direct transfer eauipment is adeauatelv
designed and has sufficient structural
strength and compatibility with the waste(s)
to be transferred to ensure that it will not
collapse, rupture or fail.
At a minimum.
this assessment must consider the fo1lowir~q~:
iL
Design standard(s).
if available,
according to which the direct transfer
equipment was constructed
~jJJ.
Hazardous characteristics of the
waste(s) that have been or will be
handled;
iii) Existing corrosion protection measures
~jyj Documented aae of the eauipment,
if
available,
(otherwise. an estimate of
the age);
and
yj
Results of a leak test or other
integrity examination such that the
effects of temperature variations, vapor
pockets,
cracks.
leaks,
corrosion and
erosion are accounted for.
~
If.
as a result of the assessment specified
above,
the direct transfer equipment is found
to be leaking or unfit for use, the owner or
operator shall com~lvwith the requirements
of 35 Iii. Ada.
Code 725.296(a)
and
(b).
11.
Inspections and recordkee~ing.
~j.
The owner or operator shall inspect at least
once each operating hour when hazardous waste
is being transferred from the transport
vehicle
(container) to the BIF:
ii
Overfill/spill control equipment
(e.g.,
waste—feed cutoff systems, bv~ass
systems and drainage systems) to ensure
that it is in aood working order
128—734
265
jjj
The above ground portions of the direct
transfer
equipment
to
detect
corrosion.
erosion or releases of waste
(e.g.. wet
spots. dead vegetation);
and
iii) Data aathered from monitoring eauipment
and
leak-detection
equipment.
(e.g..
pressure
and
temperature
gauaes)
to
ensure
that
the
direct
transfer
eaui~mentis being operated according to
its
design.
p1
The owner or oPerator shall inspect cathodic
protection
systems,
if
used, to ensure that
they are functioning properly according to
the schedule provided bY 35 Ill.
Ada. Code
725.295(b):
Qj~
Records of inspections made under this
subsection must be maintained in -the
operating record at the facility, and
available for inspection for at least
3 years
from the date of the inspection.
4j.
Design and installation of new ancillary
equipment.
Owners and operators shall comply with
the requirements of 35 Ill.
Ada. Code 725.292.
~j
Response to leaks
or. spills.
Owners and oPerators
shall comply with the requirements of
35
Ill. Ada.
Code 725.296.
~j
Closure.
Owners and operators shall comply with
the requirements of 35
Ill. Ada. Code 725.297,
except for 35 Ill. Ada. Code 725.297 (c) (2)
throucih
(cI (4).
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section 726.212
Regulation of Residues
-A residue derived from the burning or processing of hazardous
waste in a BIF is not excluded from the definition of a hazardous
waste under 35 Ill.
Ada. Code 721.104(b)(4).
(7) or
(8) unless
the device and the owner or operator meet the following
requirements:
.~j
The device meets the following criteria~
128—735
266
..3j.
Boilers.
Boilers must burn at least 50
coal on a
total heat input or mass basis, whichever results
in the areater mass feed rate of coal
21
Ore or mineral furnaces.
Industrial furnaces
subject to 35 Ill.
Ada. Code 721.104(b) (7) must
process at least 50
by weight normal,
nonhazardous
raw
materials
IL
Cement
kilns.
Cement
kilns
must
process
at
least
50
by weiaht normal cement-production raw
materials
~j
The owner or operator
demonstrates
that
the
hazardous
waste does not significantly affect the residue by
demonstrating conformance with -either of the following
criteria:
3j
Comparison of waste—derived residue with normal
residue.
The
waste—derived
residue
must
not
contain
35
Ill.
Ada.
Code
721.Appendix
H
constituents
(toxic constituents) that could
reasonably be attributable to the hazardous waste
at concentrations significantly higher than in
residue—generated without burning or processing of
hazardous waste,
using the following procedure.
Toxic compounds that could reasonably be
attributable to burning or processing the
hazardous
waste
(constituents
of
concern)
include
toxic
constituents
in
the
hazardous
waste.
and
the
organic compounds listed in 35 Ill. Ada. Code
72l.Ap~endixH that may be PICs.
Sampling and
analyses must be in conformance with procedures
prescribed in Test Methods for Evaluating Solid
Waste, Physical/Chemical Methods,
incorporated by
reference in 35
Ill. Ada. Code 720.111(a).
~j.
Normal residue.
Concentrations of toxic
constituents
of
concern
in
normal
residue
must be determined based on analyses of a
minimum of 10 samples representing
p
minimum
of 10 days of operation.
Composite samples
may be used to develop a sample for analysis
provided that the com~ositingperiod does not
exceed 24 hours.
The upper tolerance limit
(at 95
confidence with a 95
proportion of
the sample distribution)
of the concentration
in the normal residue shall be considered the
statistically-derived concentration in the
normal residue.
If chanaes in raw materials
or fuels reduce the statistically-derived
concentrations of the toxic constituents of
128—736
267
concern
in
the
normal
residue,
the
statistically-derived
concentrations
must
be
revised
or
statistically—derived
concentrations
of
toxic
constituents
in
normal
residue
must
be
established
for
a
new
mode
of
operation
with
the
new
raw
material
or fuel.
To determine the u~~ertolerance
limit
in
the
normal
residue,
the
owner
or
operator shall use statistical procedures
prescribed
in
“Statistical
Methodology
for
Bevill
Residue
Determinations”
in
Appendix
I
(“eve”).
p1
Waste—derived
residue.
Waste
derived
residue
must be sampled and analyzed as often as
necessary
to
determine
whether
the
residue
generated during each 24—hour period has
concentrations of toxic constituents that are
higher than the concentrations established
for the normal residue under subsection
(b) (1) (A).
If so. hazardous waste burning
has significantly affected the residue and
the residue is not excluded from the
definition of “hazardous waste”.
Concentrations of toxic constituents in
waste—derived residue must be determined
based on analysis of one or more samples
obtained
over
a
24-hour
period.
Multiple
samples may be analyzed, and multiple samples
may be taken to form a composite sample for
analysis provided that the sampling period
does
not
exceed
24
hours.
If
more
than
one
sample is analyzed to characterize waste—
derived
residues
aenerated
over
a
24—hour
period, the concentration of each toxic
constituent must be the arithmetic mean of
the concentrations in the samples.
No
results can be disregarded;
or
21
Comparison of waste—derived residue concentrations
with health-based limits.
~
Nonmetal constituents.
The concentrations of
nonmetal toxic constituents of concern
(specified in subsection
(b)(1))
in the
waste—derived
residue
must
not
exceed
the
health-based levels specified in Appendix G.
If
a
health-based
limit
for
a
constituent
of
concern is not listed in Appendix G. then a
limit of 0.002 ua/ka or the level of
detection (using analytical procedures
prescribed in SW-846,
incorporated by
128—737
268
reference
in
35
Ill.
Ada.
Code
720.111),
whichever is higher, must be used;
and
p1
Metal constituents.
The concentration of
metals in an extract obtained using the
TCLP
test
must
not
exceed
the
levels-
specified
in
Appendix
G:
and
,Qj
Sampling
and
analysis.
Wastewater-derived
residue
must
be
sam~1ed and
analyzed
as
often
as
necessary
to
determine
whether
the
residue
generated
during
each
24
hour
period
has
concentrations of toxic constituents which
are higher than the health—based levels.
Concentrations of concern in the wastewater—
~i~ed
residue must be determined based on
analysis of one or more samples obtained over
a 24-hour period.
Multiple samples may be
analyzed.
and multiple samples may be taken
to form a composite for analysis provided
that the sampling period does not exceed 24
hours.
If more than one sample
is analyzed
to characterize waste—derived residues
generated over a 24 hour period, the
concentration of each toxic constituent
is
the arithmetic mean of the concentrations of
the samples.
No results can be disregarded
and
~j
Records sufficient to document compliance with the
provisions of this Section must be retained until
closure of the BIF unit.
At a minimum, the following
must be recorded:
fl
Levels of constituents in 35 Ill. Ada. Code
721.Appendix H that are present in waste-derived
residues
21
If the waste-derived residue is compared with
normal residue under subsection
(b) (1):
~j
The
levels
of
constituents
in
35
Ill.
Ada.
Code 721.Appendix H that are present in
normal residues;
and
p1
Data
and
information,
including
analyses
of
samples
as
necessary,
obtained
to
determine
if changes in raw materials or fuels would
reduce the concentration of toxic
constituents of concern in the normal
residue.
128—7 38
269
(Source:
Added at 16 Ill.
Reg.
,
effective
)
Section
726.219
Extensions
of
Time
The owner or operator may request a case—by—case extension of
time to extend any time limit provided by Section 726
•
203 (c).
The
operator
shall
file
a
petition
for
a
RCRA
variance
pursuant
to 35 Ill. Ada. Code 104.
The Board will grant the variance if
compli~ncewith the time limit is not practicable for reasons
beyond the control of the owner or operator.
~j
In granting an extension,
the Board will apply
conditions
as
the
facts
warrant
to
ensure
timely
compliance with the requirements of Section 726.203 and
that the facility operates in a manner that does not
pose a hazard to human health and the environment
~j
When an owner and operator request an extension of time
to
enable
them
to
obtain
a
RCRA permit because the
facility cannot meet the HC limit of Section
726.204(c):
jj
The Board will,
in considering whether to ~rant
the extension:
~
Determine whether the owner and oPerator have
submitted in a timely manner a complete Part
B permit application that includes
information required under
35 Ill.
Ada. Code
703.208(b);
and
p1
Consider whether the owner and operator have
made a good faith effort to certify
compliance with all other emission controls.
including
the
controls
on
dioxins
and
furans
of
Section
726.204(e)
and
the
controls
on
PM.
metals
and
HC1/chlorine
gas.
ii
If an extension is qranted, the Board will, as a
condition
of
the
extension,
require
the
facility
to
operate
under
flue
aas
concentration
limits on
CO and HC that, based on available information.
including
information
in
the
Part
B
permit
application, are baseline CO and HC levels as
defined
by
Section
726.204(f)
(1).
BOARD NOTE:
Derived from 40 CFR
266.103(c)
(7) (ii),
adopted
at
56
Fed.
Req.
7206.
February 21. 1991;
and 56 Fed.
Reg.
32688. July
17.
1991.
128—739
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281
Tetraethyt
Lead
78~00-2
4E-06
Thiourea
62-56-6
Totuene
~08-88’3
1E+01
Toxatihene
8001-35-2
1.1.2-Trichloroethane
79-00-5
6?-03
Trichloroethytene
79-01-6
Trichtoromonofluoromethane
75-69-4
1E+01
2.4.5-TrichLoro~ienol
95-95-4
4E+00
2.4.6-Trichlorochenol
88-06-2
6E+00
Vanadiull
aentoxide
1314-62-1
ZLQ1
Vinyl
chloride
75-01-4
(Source:
Added at 16 Iii. Reg.
,
effective
)
Section
726.Apperidix
H
Potential
PICs
for
Determination
of
Exclusion of Waste—Derived Residues
PICs
F0CXd
in
Stack
Effluents
Votatites
Semivolatites
Benzene
Bis(2-ethy(hexyt)phthatate
Totuene
Naphthatene
Carbon tetrachioride
PhenoL
Chloroform
Diethyl phthatate
Kettylene
chloride
Butyl
benzvl
phthalate
Trichloroethylene
2.4-Dimethytphenol
Tetrachloroethylene
o-Dichtorobenzene
1.1.1-Trichloroethane
m-Dichtorobenzene
Chlorobenzene
p-DichLorobenzene
cis-1 .4-Dichloro-2-butene
Hexachlorobenzene
Brcmochtoromethane
2.4.6-Trichtproøbenot
BramodichLoromethane
F
luoranthene
Broinoform
o-Ni
troahenot
Broinomethane
1 .2.4-Trichtorobenzene
Methytene
bromide
o-Chtorophenot
Methyl ethyL ketone
Pentach
torodieno I
Pyrene
Dimethyl
phthatate
Mononi trobenzene
2.6-Toluene
diisocyanate
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section
726.Appendix
I
Methods
Manual
for
Compliance
with
BIF
Regulations
See
“Methods
Manual for Compliance with BIF Regulations”.
This
document
is
available
from
two
sources.
It
is available through
NTIS,
incorporated
by
reference
in
35
Iii.
Adm.
Code
720.111.
It
is
also
available
as
40
CFR
266.
Appendix
IX,
adopted
at
56
Fed.
Req.
32688, July 17.
1991 and amended at 56 Fed.
Reg. 42511.
Auaust 27,
1991, which
is
incorporated
by
reference.
This
incorporation
includes
no
future
editions
or
amendments..
(Source:
Added at 16 Ill. .Reg.
,
effective
)
128—75 1
282
Section 726.Appendix J
Guideline on Air quality Models
See
“Guideline
on
Air
Quality
Models
(Revised)”..
This
document
is_available
from
two
sources.
It
is
available
through
NTIS,
incorporated by reference in 35
Ill. Ada. Code 720.111.
It is
also
available
as
40
CFR
266,
Appendix
X.
adopted
at
56
Fed.
Reg.
32688. July 17.
1991 and amended at 56 Fed. Reg.
42511. August
27.
1991, which is incorporated by reference.
This incorporation
includes no future editions or amendments.
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section
726.A~~endixK
Lead-Bearing
Materials
That
May
be
Processed
in
Exempt
Lead
Smelters
~ì
Exempt Lead—Bearing Materials When Generated or
Originally
Produced
By
Lead-Associated
Industries.
BOARD NOTE:
Lead-associated industries are lead
smelters, lead—acid battery manufacturing and lead
chemical manufacturing
(e.g. manufacturing of lead
oxide or other lead compounds).
Acid
dump/fill
solids
Sum~mud
Materials
from
laboratory
analyses
Acid
filters
Baghouse
bags
Clothing
(e.g..
coveralls,
aprons,
shoes,
hats,,
gloves)
SweePings
Air filter bags and cartridges
Respiratory cartridge filters
Shop abrasive
Stacking boards
Waste shipping containers
(e.g. cartons
bags,
drums, cardboard)
Paper hand towels
128—752
283
Wiping rags and sponges
Contaminated ~allets
Water treatment sludges,
filter cakes,
residues,
and
solids
Emission control dusts, sludges,
filter
cakes,
residues,
and
solids
from
lead—associated
industries
(e.g. R069 and D008
wastes)
Spent
grinds,
posts
and
separators
Spend batteries
Lead oxide and lead oxide residues
Lead plates and groups
Scent battery cases,
covers, and vents
Pasting belts
Water filter media
Cheesecloth from pasting rollers
Pasting additive bans
Asphalt paving materials
~j
Exempt Lead—Bearing Materials When Generated or
Originally Produced By AnY Industry
Charging lumpers and clips
Platen abrasive
Fluff from lead wire and cable casings
Lead-based pigments and compounding ~iqment dust
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section
726.Appendix
L
Nickel
or
Chromium-Bearing
Materials
that
may
be
Processed
in
Exempt
Nickel-
Chromium Recovery Furnaces
128—753
284
~J-
Exempt Nickel or chromium—Bearing Materials when
Generated by Manufacturers or Users of Nickel, Chromium
or Iron.
Baghouse
bags
Raney nickel catalyst
Floor sweepings
Air filters
Electroplating bath filters
Wastewater filter media
Wood Pallets
Disposable clothing (coveralls, aprons,
hats,
and
gloves)
Laboratory samples and spent chemicals
Shipping containers and plastic liners from
containers or vehicles used to transport
nickel
or chromium—containing wastes
Respirator cartridge filters
Paper hand towels
~
Exempt Nickel or Chromium-Bearing Materials when
Generated by Any Industry
Electroplating wastewater treatment sludges
(F006)
Nickel and/or chromium—containing solutions
Nickel and/or chromium—containing catalysts
Nickel—cadmium and nickel—iron batteries
Filter cake from wet scrubber system water
treatment plants in the specialty steel industry
Filter cake from nickel-chromium alloy pickling
operations
(Source:
Added at 16 Ill. Reg.
,
effective
)
128—754
Cl
4-’
(C
0
0)
~
041
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4.’
(C
-p
-~-~
CIOIOICIOIOI
C
0I0I0I0l0I~
~
I~
~
0)
r~I
-s--I
(Ii
4-.’
0
U)
L
0)
414.4
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~
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0-J05a’I0-I°~0505I05~~
w
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-
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4—’
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0
11)
4*(
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4-SI
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1-’
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I
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00CC
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.
.
‘
_i_s
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(C
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xx
to
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w
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050-0.
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286
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE
G:
WASTE DISPOSAL
CHAPTER I:
POLLUTION CONTROL BOARD
SUBCHAPTER
C:
HAZARDOUS WASTE OPERATING REQUIREMENTS
PART 728
LAND DISPOSAL RESTRICTIONS
SUBPART
A:
GENERAL
Purpose, Scope and Applicability
Definitions
Dilution Prohibited as a Substitute for Treatment
Treatment Surface Impoundment Exemption
Procedures for case—by—case Extensions to an Effective
Date
728.106
Petitions to Allow Land Disposal of a Waste Prohibited
under Subpart C
728.107
Waste Analysis and Recordkeeping
728.108
Landfill and Surface Impoundment Disposal Restrictions
(Repealed)
728.109
Special Rules for Characteristic Wastes
SUBPART C:
PROHIBITION ON lAND DISPOSAL
Section
728.130
728. 131
728. 132
728.133
728.134
728.135
728.139
Section
728.140
728.141
728.142
728.143
728.144
Section
728.150
Appendix A
Appendix B
Appendix C
Appendix D
Appendix E
Waste Specific Prohibitions
--
Solvent Wastes
Waste Specific Prohibitions
——
Dioxin-Containing Wastes
Waste Specific Prohibitions
—-
California List Wastes
Waste Specific Prohibitions
——
First Third Wastes
Waste Specific Prohibitions
--
Second Third Wastes
Waste Specific Prohibitions
--
Third Third Wastes
Statutory Prohibitions
SUBPART D:
TREATMENT STANDARDS
Applicability of Treatment Standards
Treatment Standards expressed as Concentrations in
Waste Extract
Treatment Standards expressed as Specified Technologies
Treatment Standards expressed as Waste Concentrations
Adjustment of Treatment Standard
SUBPART E:
PROHIBITIONS ON STORAGE
Prohibitions on Storage of Restricted Wastes
Toxicity Characteristic Leaching Procedure
(TCLP)
Treatment Standards
(As concentrations in the
Treatment Residual Extract)
List of Halogenated Organic Compounds
Organometallic Lab Packs
Organic Lab Packs
Section
728.101
728.102
728.103
728.104
728.105
128—756
287
Appendix F
Technologies to Achieve Deactivation of
Characteristics
Appendix G
Federal Effective pates
Appendix H
National Capacity LDR Variances for UIC Wastes
Table A
Constituent Concentrations in Waste Extract
(CCWE)
Table B
Constituent Concentrations in Wastes
(CCW)
Table C
Technology Codes and Description of Technology—Based
Standards
Table D
Technology-Based Standards by RCRA Waste Code
Table ~
Standards for Radioactive Mixed Waste
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the Environmental Protection Act
(Ill.
Rev.
Stat.
1989,
ch.
111½, pars.
1022.4 and 1027).
SOURCE:
Adopted in R87-5 at 11 Ill. Reg.
19354,
effective
November 12,
1987; amended in R87—39 at 12
Ill. Reg.
13046,
effective July 29,
1988; amended in R89—l at 13
Ill. Reg.
18403,
effective November 13,
1989; amended in R89—9 at 14 Ill.
Reg.
6232,
effective April 16,
1990; amended in R90—2 at 14
Ill.
Reg.
14470,. effective August 22,
1990; amended in R90-l0 at 14
Ill.
Reg.
16508, effective September 25,
1990;
amended in R90—11 at 15
Ill.
Reg.
9462, effective June 17,
1991;
amended in R91—13 at 16
Ill.
Reg.
,
effective
SUBPART A:
GENERAL
Section 728.107
Waste Analysis and Recordkeeping
a)
Except as specified in Section 728.132 or 728.143
.
if
a generator’s waste is listed in 35
Ill. Adm. Code
721.Subpart
D, the generator shall test the generator’s
waste,
or test an extract developed using the test
method described in Appendix A35 Ill.
Adm. Code
721.Ap~endixB, or use knowledge of the waste, to
determine if the waste is restricted from land disposal
under this Part.
Except as specified in Section
728.132.
if a
generator’s
waste
exhibits
one
or
more
of
the
characteristics
set
out
at
35
Ill.
Adm.
Code
721.Subpart
C. the generator shall test an extract
using the test method described in AppendixI
(“eye”),
or use knowledge of the waste,
to determine if the
waste is restricted from land disposal under this Part.
1)
If
a
generator
determines
that
the
generator
is
managing a restricted waste under this Part and
determines
that
the
waste
does
not
meet
the
applicable
treatment
standards
set
forth
in
Subpart
D
or
exceeds
the applicable prohibition
levels set forth in Section 728.132 or 728.139,
with each shipment of waste the generator shall
128—75~
288
notify the treatment or storage facility in
writing of the appropriate treatment standard set
forth in Subpart D and any applicable prohibition
levels set forth in Section 728.132 or 728,139.
The notice must include the following information:
A)
USEPA Hazardous Waste Number;
B)
The corresponding treatment standards for
wastes F001—F005,
F039 and wastes prohibited
pursuant to Section 728.132 or Section
3004(d)
of the Resource Conservation and
Recovery Act, referenced in Section 728.139.
Treatment standards for all other restricted
wastes must either be included, or be
referenced as above, or by including on the
notification the subcategory of the
waste-,
the
treatability
group(3)
of
the
waste(s)~,app1icablewastewater or
nonwastewater
(as defined in Section 728.102)
category, the applicable subdivisions made
within a waste code based on waste—specific
criteria
(such as D003, reactive cyanides),
and the Section and subsection where the
applicable treatment standards appear~.
Where the applicable treatment standards are
expressed as specified technologies in
Section 728.142,
the applicable five-letter
treatment code found in Table C (e.g., INCIN,
WETOX)
also must be listed on the
notification.
C)
The manifest number associated with the
shipment of waste; and
D)
Waste analysis data, where available.
2)
If a generator determines that the generator is
managing a restricted waste under this Part,
and
determines that the waste can be land disposed
without further treatment, with each shipment of
waste the generator shall submit, to the
treatment, storage or land disposal facility, a
notice and a certification stating that the waste
meets the applicable treatment standards set forth
in Subpart D and the applicable prohibition levels
set forth in Section 728.132 or 728.139.
A)
The notice must include the following
information:
i)
USEPA Hazardous Waste Number;
128—758
289
ii)
The corresponding treatment standards
for
wastes
F001-F005,
F039
and
wastes
prohibited
pursuant
to
Section
728.132
or
Section
3004(d)
of
the
Resource
Conservation
and
Recovery
Act,
referenced
in
Section
728.139.
Treatment
standards
for
all
other
restricted wastes must either ~g
included
or
be
referenced
as
above,
or
by including on the notification tI~e
suboategory
of
thc
waste,
the
treatability
group(s)
of
thc
waste(s)
,
wastewater
or
nonwastewater
(as
defined in Section 728.102) category,
the applicable subdivisions made within
p waste code based on waste—specific
criteria
(such as D0035 reactive
cyanides).
and
the
Section
and
subsection where the applicable
treatment standards appear~. Where the
applicable treatment standards are
expressed as specified technologies in
Section 728.142, the applicable
five—letter treatment code found in
Table C
(e.g.,
INCIN, WETOX)
also must
be listed on the notification.
iii) The manifest number associated with the
shipment of waste;
iv)
Waste analysis data, where available.
B)
The certification must be signed by an
authorized representative and must state the
following:
I certify under penalty of law that I
personally
have
examined
and
am familiar
with the waste through analysis and
testing or through knowledge of the
waste to support this certification that
the waste complies with the treatment
standards specified in 35 Ill. Adm. Code
728.Subpart D and all applicable
prohibitions set forth in 35 Ill.
Adm.
Code 728.132, 728.139 or Section 3004(d)
of the Resource Conservation and
Recovery Act.
I believe that the
information
I submitted is true,
accurate and complete.
I am aware that
there are significant penalties for
128—759
290
submitting a false certification,
including the possibility of a fine and
imprisonment.
3)
If a generator’s waste is subject to an exemption
from a prohibition on the type of land disposal
method utilized for the waste (such as, but not
limited to, a case—by—case extension under Section
728.105,
an exemption under Section 728.106, an
extension under Section 728.101(c) (3) or a
nationwide capacity variance under 40 CFR
268.Subpart C (1989), with each shipment of waste,
the generator shall submit a notice with the waste
to the facility receiving the generator’s waste,
stating that the waste is not prohibited from land
disposal.
The notice must include the following
information:
A)
EPA hazardous waste number:
B)
The corresponding treatment standards for
wastes FOOl-FOOS,
F039 and wastes prohibited
pursuant to Section 728.132 or Section
3004(d) of the Resource Conservation and
Recovery Act, referenced in Section 728.139.
Treatment standards for all other restricted
wastes must either be included, or be
referenced as above,
or by including on the
notification the aubcategory of the waste,
the treatability group(s)
of the
waste(s) ,wastewater or nonwastewater
(as
defined in Section 728.102) category, the
applicable subdivisions made within a waste
code based on waste-specific criteria
(such
as D003, reactive cyanides),
and the Section
and subsection where the applicable treatment
standards appear~. Where the applicable
treatment standards are expressed as
specified technologies in Section 728.142,
the applicable five-letter treatment code
found in Table C
(e.g.,
INCIN, WETOX) also
must be listed on the notification.
C)
The manifest
number
associated with the
shipment of waste;
D)
Waste analysis data,
where available, and
E)
The date the waste is subject to the
prohibitions
4)
If a generator is managing a prohibited waste in
128—760
291
tanks or containers regulated under 35 Ill. Adm.
Code 722.134, and is treating such waste in such
tanks or containers to meet applicable treatment
standards under Subpart D, the generator shall
develop and follow a written waste analysis plan
which describes the procedures the generator will
carry out to comply with the treatment standards.
The plan must be kept on—site in the generator’s
records,
and
the
following
requirements
must
be
met:
A)
The waste analysis plan must be based on a
detailed chemical and physical analysis of a
representative sample of the prohibited
waste(s) being treated, and contain all
information necessary to treat the waste(s)
in accordance with the requirements of this
Part, including the selected testing
frequency.
B)
Such plan must be filed with the Agency a
minimum of 30 days prior to the treatment
activity, with delivery verified.
C)
Wastes shipped off-site pursuant to this
subsection must comply with the notification
requirements of Section 728.107(a) (2).
5)
If a generator determines whether the waste is
restricted based solely on the generator’s
knowledge of the waste, the generator shall retain
all supporting data used to make this
determination on—site in the generator’s files.
If a generator determines whether the waste is
restricted based on testing the waste or an
extract developed using the test method described
in Appendix A, the generator shall retain all
waste analysis data on site in the generator’s
files.
6)
If a generator determines,
subsequent to the point
of generation, that the generator is managing a
restricted
waste which is excluded from the
definition
of hazardous or solid waste or exempt
from regulation as a RCRA hazardous waste under 35
Ill. Adm. Code 721.102
-
721.106, the generator
shall place,
in the facility’s file,
a one-time
notice stating such generation,
subsequent
exclusion from the definition of hazardous or
solid waste or exemption from regulation as a RCRA
hazardous waste, and the disposition of the waste.
128—76 1
292
~
Generators shall retain on—site
a copy of. all
notices, certifications, demonstrations, waste
analysis data and other documentation produced
pursuant to this Section for at least five years
from the date that the waste that is the subject
of such documentation was last sent to on—site or
off—site treatment storage or disposal.
The five
year record retention period is automatically
extended during the course of any unresolved
enforcement action regarding the regulated
activity or as requested by the Agency.
~g
requirements of this subsection a~~lv
to solid
wastes even when the hazardous characteristic is
removed prior to disposal.
or when the waste is
excluded
from
the
definition
of
hazardous
or
solid
waste under 35
Ill.
Adni.
Code 721.102
-
721.106.
or exempted from regulation as a
RCRA
hazardous
waste subsequent to the point of generation.
~7-~)If a generator is managing a lab pack that
contains wastes identified in Appendix D and
wishes to use the alternative treatment standard
under Section 728.142, with each shipment of waste
the generator shall submit a notice to the
treatment facility in accordance with subsection
(a) (1).
The generator shall also comply with the
requirements in subsections
(a) (5) and
(a) (6), and
shall submit the following certification, which
must be signed by an authorized representative:
I certify under penalty of law that I
personally have examined and am familiar with
the waste and that the lab pack contains only
the wastes specified in 35 Ill. Adm. Code
728.Appendix D or solid wastes not subject to
regulation under 35 Ill.
Adm. Code 721.
I am
aware that there are significant penalties
for submitting a false certification,
including the possibility of fine or
imprisonment.
~)
If a generator is managing a lab pack that
contains organic wastes specified in Appendix E
and wishes to use the alternate treatment
standards under Section 728.142, with each
shipment of waste the generator shall submit a
notice to the treatment facility in accordance
with subsection
(a) (1).
The generator also shall
comply with the requirements in subsections
(a) (5)
and
(a) (6), and shall submit the following
certification which must be signed by an
authorized representative:
128—762
293
I certify under penalty of law that I
personally have examined and am familiar with
the waste through analysis and testing or
through knowledge of the waste and that the
lab pack contains only organic waste
specified in 35 Ill. Adm. Code 728.Appendix E
or
solid
wastes
not
subject
to
regulation
under 35
Ill. Adm. Code
721.
I
am
aware
that
there are significant penalties for
submitting a false certification, including
the possibility of fine or imprisonment.
9~Q)
Small quantity generators with tolling agreements
pursuant to 35 Ill.
Adin.
Code 722.120(e)
shall
comply with the applicable notification and
certification requirements of subsection
(a)
for
the initial shipment of the waste subject to the
agreement.
Such generators shall retain on—site a
copy of the notification and certification,
together with the tolling agreement,
for at least
three years after termination or expiration of the
agreement.
The three—year record retention period
is automatically extended following notification
pursuant to Section 31(d)
of the Environmental
Protection Act, until either any subsequent
enforcement action is resolved, or the Agency
notifies the generator documents need no be
retained.
b)
Treatment facilities shall test their wastes according
to the frequency specified in their waste analysis
plans as required by 35 Ill. Adm. Code 724.113 or
725.113.
Such testing must be performed as provided in
subsections
(b) (1),
(b) (2) and
(b) (3).
1)
For wastes with treatment standards expressed as
concentrations in the waste extract
(Section
728.141), the owner or operator of the treatment
facility shall test the treatment residues or an
extract of such residues developed using the test
method described in Appendix A to assure that the
treatment residues or extract meet the applicable
treatment standards.
2)
For wastes prohibited under Section 728.132 or
728.139 which are not subject to any treatment
standards under Subpart D, the owner or operator
of the treatment facility shall test the treatment
residues according to the generator testing
requirements specified in Section 728.132 to
assure
that
the
treatment
residues
comply with the
128—763
294
applicable prohibitions.
3)
For wastes with treatment standards expressed as
concentrations in the waste (Section 728.143), the
owner or operator of the treatment facility shall
test the treatment residues (not an extract of
such residues)
to assure that the treatment
residues meet the applicable treatment standards.
4)
A notice must be sent with each waste shipment to
the land disposal facility which includes the
following information:
A)
USEPA
Hazardous
Waste
Number;
B)
The corresponding treatment standards for
wastes F0O1—F005, F039 and wastes prohibited
pursuant to Section 728.132 or Section
3004(d) of the Resource Conservation anif
Recovery Act, referenced in Section 728.139.
Treatment standards for all other restricted
wastes must either included,
or be be
referenced as above,
or by including on the
notification the subcategory of the waste,
th~treatability -group(s) of the
waste(s) ,wastewater or nonwastewater
(as
defined in Section 728.102)
category, the
applicable subdivisions made within
a waste
code based on waste—specific criteria
(such
as D003,
reactive cyanides),
and the Section
and subsection where the applicable treatment
standards appear~. Where the applicable
treatment standards are expressed as
specified technologies in Section 728.142,
the applicable five-letter treatment code
found in Table C (e.g.,
INCIN, WETOX)
also
must be listed on the notification.
C)
The manifest number associated with the
shipment of waste; and
D)
Waste analysis data,
where available.
5)
The treatment facility shall submit a
certification with each shipment of waste or
treatment residue of a restricted waste to the
land disposal facility stating that the waste or
treatment residue has been treated in compliance
with the treatment standards specified in Subpart
D and the applicable prohibitions set forth in
Section 728.132 or 728.139.
128—764
295
A)
For wastes with treatment standards expressed
as concentrations in the waste extract or in
the waste (Sections 728.141 or 728.143), or
for wastes prohibited under Section 728.132
or 728.139 which are not subject to any
treatment standards under Subpart
D, the
certification must be signed by an authorized
representative and must state the following:
I certify under penalty of law that
I
have personally examined and am familiar
with the treatment technology and
operation of the treatment process used
to support this certification and that,
based on my inquiry of those individuals
immediately responsible for obtaining
this information,
I believe that the
treatment process has been operated and
maintained properly so as to comply with
the performance levels specified in 35
Ill. Adm. Code 728.Subpart D and all
applicable prohibitions set forth in 35
Ill. Adm. Code 728.132 or 728.139 or
section 3004(d)
of the Resource
Conservation and Recovery Act without
impermissible dilution of the prohibited
waste.
I am aware that there are
significant penalties for submitting a
false certification, including the
possibility of fine and imprisonment.
B)
For wastes with treatment standards expressed
as technologies (Section 728.142), the
certification must be signed by an authorized
representative and must state the following:
I certify under penalty of law that the
waste has been treated in accordance
with the requirements of 35 Ill. Adm.
Code 728.142.
I am aware that there are
significant
penalties
for
submitting
a
false
certification,
including
the
possibility
of
fine
and
imprisonment.
C)
For wastes with treatment standards expressed
as concentrations in the waste pursuant to
Section 728.143,
if compliance with the
treatment standards in Subpart D is based in
part or in whole on the analytical detection
limit alternative specified in Section
728.143(c), the certification also must state
the following:
128—765
296
I certify under penalty of law that I
have personally examined and am famil.
with the treatment technology and
operation of the treatment process us’
to support this certification and tha
based on my inquiry of those individu
immediately responsible for obtaining
this information,
I believe that the
nonwastewater organic constituents ha’
been treated by incineration in units
operated in accordance with 35 Iii.
A’~
Code 724.Subpart 0)
or 35 Ill. Adm. C
725.Subpart 0, or by combustion in fu~
substitution units operating in
accordance with applicable technical
requirements, and
I have been unable
t
detect the nonwastewater organic
constituents despite having used best
good faith efforts to analyze for suci
constituents.
I am aware that there ~
significant penalties for submitting ~
false certification,
including the
possibility of fine and imprisonment.
6)
If the waste or treatment residue will be furthE
managed at a different treatment or storage
facility,the treatment,
storage or disposal
facility sending the waste or treatment residue
off-site must comply with the notice and
certification requirements applicable to
generators under this Section.
7)
Where the wastes are recyclable materials used
i
a manner constituting disposal subject to the
provisions of 35 Ill. Adm. Code 726.120(b),
regarding treatment standards and prohibition
levels, the owner or operator of a treatment
facility
(i.e.
the recycler)
is not required to
notify the receiving facility pursuant to
subsection
(b) (4)’.
With each shipment of such
wastes the owner or operator of the recycling
facility shall submit a certification described
subsection
(b) (5), and a notice which includes t
information listed in subsection
(b) (4)
(except
the manifest number) to the Agency.
The recycli
facility also shall keep records of the name and
location of each entity receiving the hazardous
waste—derived product.
c)
Except where the owner or operator is disposing of an
waste that is a recyclable material used in a manner
128—766
297
constituting disposal pursuant to 35 Ill.
Adm.
Code
726.120(b), the
owner or operator of any land disposal
facility disposing any waste subject to restrictions
under this Part shall:
1)
Have copies of the notice and certification
specified
in
subsection
(a)
or
(b),
and
the
certification
specified
in
Section
728.108
if
applicable.
2)
Test the waste, or an extract of the waste or
treatment residue developed using the test method
described in Appendix A or using any methods
required by generators under Section 728.132, to
assure that the wastes or treatment residues are
in compliance with the applicable treatment
standards set forth in Subpart D and all
applicable prohibitions set forth in Sections
728.132 or 728.139.
Such testing must be
performed according to the frequency specified in
the facility’s waste analysis plan as required by
35 Ill.
Adm. Code 724.113 or 725.113.
3)
Where the owner or operator is disposing of any
waste that is subject to the prohibitions under
Section 728.133(f)
but not subject to the
prohibitions set forth in Section 728.132, the
owner or operator shall ensure that such waste
is
the subject of a certification according to the
requirements of Section 728.108 prior to disposal
in a landfill or surface impoundment unit,
and
that such disposal is in accordance with the
requirements of Section 728.105(h).(2).
The same
requirement applies to any waste that is subject
to the prohibitions under Section 728.133(f)
and
also is subject to the statutory prohibitions in
the codified prohibitions in Section 728.139 or
Section 728.132
4)
Where the owner or operator is disposing of any
waste that is a recyclable material used in a
manner constituting disposal subject
to
the
provisions of 35 Ill. Adm.
Code
726.120(b),
the
owner
or
operator
is
not
subject
to
subsections
(c)
(1)
through
(3)
with
respect
to
such
waste.
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
Section 728.109
Special Rules for Characteristic Wastes
a)
The initial generator of a solid waste shall determine
128—7
67
298
each USEPA hazardous waste number
(waste codel
applicable to the waste in order to determine the
applicable treatment standards under Subpart D.
For
purposes of part 26Othis Part, the waste will carry
a~gwaste code designation for any applicable listing
under 35 Ill.
Adm.
Code 721.Subpart D7—snd also.
In
~ition.
the waste wili. carry one or more of the waste
code~designations under 35 Ill. Adm. Code 721.Subpart
C where the waste exhibits the relevant characteristic~
except in the case when the treatment standard for the
waste code listed in 35
I...
Adin.
Code 721.Subpart D
operates in lieu of the standard for the waste code
under 35 Ill. Adm. Code 721.Subpart
C,
as specified in
subsection
(b).
b)
Where a prohibited waste is both listed under 35 Ill.
Adm. Code 721.Subpart D and exhibits a characteristic
under 35 Ill.
Adm. Code 721.Subpart
C, the treatment
standard for the waste code listed in 35
Ill. Adm. Code
721.Subpart D will operate in lieu of the standard for
the waste code under
35 Ill. Adm. Code 72l.Subpart C,
provided that the treatment standard for the listed
waste includes a treatment standard for theconstituent
that causes the waste to exhibit the characteristic.
Otherwise, the waste must meet the treatment standards
for all applicable listed and characteristic waste
codes.
c)
In addition to any applicable standards determined from
the initial point of generation,
no prohibited waste
which exhibits a characteristic under 35 Ill. Adm. Code
721.Subpart C shall be land disposed unless the waste
complies with the treatment standards under Subpart D.
d)
Wastes that exhibit a characteristic are also subject
to Section 728.107 requirements, except that once the
waste is no longer hazardous, for each shipment of such
wastes
to
a
non-hazardous
waste
facility,
regulated
under 35 Ill. Adm.
Code
807
or 811 through 815, or
exempted under Section 21(d) (1) (i) of the Environmental
Protection Act, or similarly regulated in other States,
the initial generator or the treatment facility need
not send a Section 728.107 notification to such
facility.
In such circumstances,
a notification and
certification must be sent to the Agency, or, for out—
of-State shipments,
to the appropriate USEPA Regional
Administrator or State authorized,
pursuant to 40 CFR
271, to implement 40 CFR 268 requirements.
1)
The notification must include the following
information:
128—7 68
299
A)
The name and address of the non—hazardous
waste facility receiving the waste shipment;
B)
A description of the waste as initially
generated,
including the applicable USEPA
Hazardous Waste Number(s)
and treatability
group(s), the applicable wastewater or
nonwastewater
(as defined in Section 728.102)
category, and the subdivisions made within a
waste code based on waste—specific criteria
(such as D003. reactive cvanides)
C)
The treatment standards applicable to the
waste at the initial point of generation.
2)
The certification must be signed by an authorized
representative and must state the language found
in Section 728.107(b) (5) (A).
(Source:
Amended at 16 Ill. Reg.
,
effective
)
Section 728.110
First Third
The Board incorporates by reference 40 CPR 268.10
(1991).
This
Section incorporates no later editions or amendments.
(Source:
Added at
16 Ill.
Reg.
,
effective
Section 728.111
Second Third
The Board incorporates by reference 40 CFR 268.11
(1991).
This
Section incorporates no later editions or amendments.
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section 728.112
Third Third
The Board incorporates bY reference 40 CFR 268.12
(1991).
This
Section incorporates no later editions or amendments.
(Source:
Added at 16 Ill. Reg.
,
effective
)
Section 728.113
Newly Listed Wastes
The Board incorporates by reference 40 CFR 268.13
(1991).
This
Section incorporates no later editions or amendments.
(Source:
Added at 16 Ill. Reg.
,
effective
128—769
300
)
Section 728.133
a)
Waste Specific Prohibitions
—-
First Third
Wastes
(nonwastewater)
wastes specified in Section 728.143(a)
and
Table B
K008
wastes specified in Section 728.143(a)
and
Table B
wastes specified in Section 728.143(a)
and
Table B
(nonwastewater)
nonwastewaters specified in Section
728.143(a)
and Table B
(nonwastewater)
(nonexplosive)
(nonwastewater)
(nonwastewater)
(nonwastewaters containing less than 15
zinc)
(non CaSO4)
(nonwastewater)
(solvent washes),
nonwastewaters specified in Section
728.143(a)
and Table B
(wastewater)
(nonwastewater,
low arsenic subcategory
—-
less than 1
total arsenic
K102
(wastewater)
The wastes specified in 35 Ill. Adm. Code 721.132 as
USEPA hazardous wastes numbers listed below are
prohibited from land disposal (except in an injection
well).
Until August
7, 1~90,K0G1 wastes containing
15
zinc or greater are prohibited from land dispgsal
pursuant to the treatment standards specified in
Cection 720.141 applicable to K061 wastes that contain
less than 15
zinc.
FO06
KO01
1(004
K015
KO16
KO18
K0.9
K020
K021
KO22
K024
K025
K030
K036
1(037
KO44
KO45
K046
KO47
KO60
KO61
KO 62
K069
K086
K087
KO99
Ki00
Ki01
KlOl
128—770
301
K102
(nonwastewater,
low arsenic subcategory
——
less than 1
total arsenic
K103
K104
b)
Effective
August
8,
1990,
tlhe
wastes
specified
in
35
Ill. Adm. Code 721.132 as USEPA Hazardous Waste Nos.
K040,
K049, K050,
K051, K052,
K061 (containing 15
zinc
or greater), and K071 a~’ej~
prohibited from land
dispbsal.
C)
Effective August
0,
1900,
tlhe wastes specified in
Section 728.110 having
a treatment standard in Subpart
D based on incineration and which are contaminated soil
and debris are prohibited from land disposal.
d)
Until
Augu~cu,
ii.iu, wa~ce3inciuaea in
~uD~eccion
ID)
and
(C)
may be disposed of in a landfill or surface
impoundment only if such unit is in compliance with the
requirements specified in 40 CFR 260.5(h) (2),
incorporated by reference in Cection 720.105.
e)
The requirements of subsection
(a),
(b),
(c) and
(d)
do
not apply if:
1)
The wastes meet the applicable standards specified
in Subpart D; or
2)
Persons have been granted an adjusted standard
pursuant to Section 728.106, with.respect to those
wastes and units covered by the petition; or
3)
Persons have been granted an extension to the
effective date of a prohibition pursuant to
Section 728.105, with respect to those wastes
covered by the extension.
f)
Until May 0,
1990, the wastes specified in Gection
728.110 for which treatment standards under Cubpart D
have not been promulgated,
including those wastes which
are subject to the statutory prohibitions of Cection
720.139 or codified prohibitions under Cection 720.132,
but not including wastes subject to a treatment
standard under Cection 720.142, are prohibited from
disposal in a landfill or surface impoundment unless
unless a demonstration and certification have been
submitted pursuant to Cection 728.108.
g)
To determine whether a hazardous waste listed in
Section 728.110 exceeds the applicable treatment
standards specified in Sections 728.131 and 728.143,
the initial generator shall test a representative
128—771
302
sample of the waste extract or the entire waste
depending on whether the treatment standards are
expressed as concentrations in the waste extract or the
waste,
or
the
generator
may
use
knowledge
of
the
waste.
If
the
waste
contains
constituents
in
excess
of
the
applicable Subpart D levels, the waste is prohibited
from land disposal and all requirements of this Part
are
applicable
except
as
otherwise
specified.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
Section 728.135
Waste Specific Prohibitions--Third Third
wastes.
a)
The following wastes are prohibited from land disposal.
1)
The wastes specified in 35 Ill. Adm.
Code 721.131
as
EPA
Hazardous
Waste
Numbers:
F002
(1,1, 2-trichloroethane)
F005 (benzene)
F005 (2—ethoxyethanol)
F005 (2—nitropropane)
F006
(wastewaters),
F019
F025
F039 (wastewaters);
2)
The wastes specified in 35 Ill. Adm. Code 721.132
as EPA Hazardous Waste Numbers:
K002
K003
K004
(wastewaters)
K005 (wastewaters)
K006
K008 (wastewaters)
KOll (wastewaters)
K013
(wastewaters)
K014
(wastewaters)
K015
(nonwastewaters)
1017
1021
(wastewaters)
1022
(wastewaters)
K025
(wastewaters)
K02 6
K02 9
(wastewaters)
1031
(wastewaters)
KO32
1033
KO34
128—772
303
K035
K041
K042
K046 (wastewaters, reactive nonwastewaters)
K04 8
(wastewaters)
1049
(wastewaters)
1050
(wastewaters)
1051
(wastewaters)
1052
(wastewaters)
1060
(wastewaters)
1061
(wastewaters)
‘and
(high
zinc
subcategory
15
zinc)
1069
(wastewaters. calcium sulfate
nonwastewaters)
K073
1083
-(waatcwatcrs)
1084
(wastewaters)
1085
1095
(wastewaters)
1096
(wastewaters)
1097
1098
1100
(wastewaters)
Kl01 (wastewaters)
K102
(wastewaters)
1105
1106
(wastewaters)
3)
The wastes specified in 35 Ill.
Adin.
Code
721.133(e)
as EPA Hazardous Waste Numbers:
Pool
P002
P003
P004
P005
P006
P007
P008
P009
POlO (wastewaters)
POll (wastewaters)
P012
(wastewaters)
P014
P015
P016
P017
P018
~,astewat
P020
P022
P023
P024
128—7
73
304
P024
P027
P028
P031
P033
P034
P036
(wastewaters)
P037
P038
(wastewaters)
P042
P045
P046
P047
P048
P049
P050
P051
P054
P056
P057
P058
P059
P060
P064
P065
(wastewaters)
P066
P067
P068
P069
P070
P072
P073
P075
P076
P077
P078
P081
P082
P084
P088
P092
(wastewaters)
P093
P095
P096
P101
P102
P103
P105
P108
P109
P110
P112
128—774
305
P113
P114
P115
P116
P118
P119
P120
P122
P123
4)
The wastes specified in 35 Ill. Adm.
Code
721.133(f) as EPA Hazardous Waste Numbers:
U001
U002
U003
U004
U005
U006
U007
U008
U009
U010
UO11
U012
U014
U015
U016
U017
U018
U019
U020
U021
U022
U023
U024
U025
U026
UO27
U029
U030
U031
U032
U033
U034
U035
U036
UO37
U038
U039
U041
U042
128—775
306
U043
U044
U045
U046
U047
U048
U049
U050
U051
U052
U053
U055
U056
UO57
U059
U060
U061
U062
U063
U064
U066
U067
U068
11070
11071
11072
U073
U074
U075
U076
U077
U078
U079
U080
U081
U082
U083
U084
U085
U086
U089
U090
U09 1
U092
U093
U094
U095
U096
U097
U098
U099
Ui01
128—776
307
U103
Ui05
U106
Ui08
Ui09
Ui10
Ui11
13112
13113
Ui14
Ui15
Ui16
U117
Ui18
Ui19
U120
.
.stewaters)
Ui21
13122
11123
Ui24
U125
U126
11127
Ui28
Ui-29
Ui30
11131
U132
Ui33
Ui34
U135
U136
(wastewaters)
Ui37
Ui38
Ui40
U141
11142
Ui43
U144
11145
U146
11147
11148
11149
13150
13151
(wastewaters)
13152
13153
11154
Ui55
Ui56
11157
128—777
308
13158
13159
13160
11161
Ui62
Ui63
U164
Ui65
Ui66
13167
11168
Ui69
U170
13171
Ui72
Ui73
13174
11176
11177
13178
Ui79
11180
Ui81
U182
11183
U184
U185
13186
Ui87
Ui8 8
13189
Ui91
11192
11193
Ui94
13196
Ui.97
U200
U201
U202
U203
U204
U205
U206
13207
13208
11209
U210
U2ii
13213
11214
13215
128— 7 78
309
11216
13217
13218
13219
13220
U222
13225
13226
13227
13228
13234
U236
U237
U238
U239
13240
13243
13244
13246
13247
13248
U249
4)
The following wastes identified as hazardous based
on a characteristic alone:
D001
D002
DO03
D004
(wastewaters)
DO05
D006
D007
D008 (except for lead materials stored before
secondary smelting)
DOO9
(wastewaters)
DOiO
DOll
DOi2
D013
DO14
D015
D016
D017
b)
The
following
wastes
are
prohibited
from
land
disposal.
The wastes specified in 35 Iii. Adm. Code 721.132 as
EPA
Hazardous
Waste
Numbers:
1048
(nonwastewaters)
1049
(nonwastewaters)
1050
(nonwastewaters)
12 8—7
79
310
1051
(nonwastewaters)
1052
(nonwastewaters)
c)
Effective Nay 8,
1992, the following wastes are
prohibited from land disposal:
1)
The wastes specified in 35
Ill.
Adm. Code 721.131
as
EPA
Hazardous
Waste Numbers:
F039 (nonwastewaters)
2)
The wastes specified in 35 Ill.
Adin. Code 721.132
as
EPA
Hazardous Waste Numbers:
1031
(nonwastewaters)
1084
(nonwastewaters)
1101
(nonwastewaters)
1102
(nonwastewaters)
K106
(nonwastewaters)
3)
The wastes specified in 35
Ill.
Adm.
Code
721.133(e) as EPA Hazardous Waste Numbers:
POlO
(nonwastewaters)
POll
(nonwastewaters)
P012
(nonwastewaters)
P036
(nonwastewaters)
P038
(nonwastewaters)
P065
(nonwastewaters)
P087
(nonwastewaters3-
P092
(nonwastewaters)
4)
The wastes specified in 35 Ill. Adm. Code
721.133(f)
as EPA Hazardous Waste Numbers:
Ui36
(nonwastewaters)
13151
(nonwastewaters)
5)
The following wastes identified as hazardous based
on a characteristic alone:
D004
(nonwastewaters)
D008
(lead materials stored before secondary
smelting)
D009
(nonwastewaters);
6)
Inorganic solids debris as defined in 35 Ill. Adm.
Code 728.102(a)(7)
(which also applies to chromium
refractory bricks carrying the EPA Hazardous Waste
Numbers 1048-1052)
7)
RCRA
hazardous wastes that contain naturally
128—780
311
occurring radioactive materials.
d)
Effective
May
8,
1992,
hazardous
wastes listed in
4-G
CFII
263.l2Sections
728.110,
728.111
or
728.112 that are
mixed radioactive/hazardous wastes, and soil or debris
contaminated with hazardous wastes listed in Sections
728.110,728.111
or 728.112 that are mixed
radioactive/hazardous wastes, are prohibited from land
disposal.
e)
Effective May 8,
1992, the wastes specified in this
Section having a treatment standard in Subpart D based
on incineration, mercury retorting, vitrification, acid
leaching.followed by chemical precipitation or thermal
recovery of metals and which are contaminated soil or
debris, are prohibited from land disposal.
h)
Between May 8,
1990,
and May 8,
1992, wastes included
in subsections
(c),
(d)
and
(e)
shall be disposed Of in
a landfill or surface impoundment only if such unit is
in compliance with the requirements specified in
Section 728.105(h) (2).
i)
The requirements of subsections
(a),
(b)’,
(c),
(d)
and
(e) do not apply if:
1)
The wastes meet the applicable standards specified
in Subpart D;
2)
Persons have been granted an exemption from a
prohibition pursuant to a petition under Section
728.106, with respect to those wastes and units
covered by the petition;
3)
The wastes meet the applicable alternate standards
established pursuant to a petition granted under
Section 728.144;
4)
Persons have been granted an extension to the
effective date of a prohibition pursuant to
Section 728.105, with respect to these wastes
covered by the extension.
j)
To determine whether a hazardous waste listed in 40
Cr11
268.10,
268.11 and 260.l2Section 728.110, 728.111 or
728.112 exceeds the applicable treatment standards
specified in Sections 728.141 and 728.143, the initial
generator shall either test a representative sample of
the waste extract or the entire waste, depending on
whether the treatment standards are expressed as
concentrations in the waste extract or the waste, or
use knowledge Of the waste.
If the waste contains
128—781
312
constituents in excess of the applicable Subpart D
levels, the waste is prohibited from land disposal, and
all requirements of this Part are applicable,
except as
otherwise specified.
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
SUBPART
D:
TREATMENT
STANDARDS
Section 728.140
Applicability of Treatment Standards
a)
A restricted waste identified in Section 728.141 may be
land disposed only if an extract of the waste or of the
treatment residue of the waste developed using the test
method Appendix A35 Ill. Adm. Code 721.Appendix B does
not exceed the value shown in Table A for any hazardous
constituent listed in Table A for that waste, with the
following exceptions:
D004,
D008,
1031,
K084,
KlOl,
1102,
POlO,
P011,
P012,
P036, P038 and U136.
Wastes
D004,
D008,
1031,
K034,
1101,
1102,
P010,
POll,
P012,
P036, P030
and Ul36These wastes may be land disposed
only if an extract of the waste or of the treatment
residue of the waste developed using either the test
method in 35111.
Adin. Code 721.Appendix A~or the test
method in
35 Ill.
Adm. Code 720.Appendix BI
(“eye”)
of
this Part does not exceed the valueconcentrations shown
in Table B~for any hazardous constituent listed in
Table A for that waste.
b)
A restricted waste for which a treatment technology is
specified under Section 728.142(a) may be land disposed
after it is treated using that specified technology or
an equivalent treatment method approved by the Agency
under the procedures set forth in Section
728.142(b).
c)
Except as otherwise specified in Section 728.143(c),
a
restricted waste identified in Section 728.143 may be
land disposed only if the constituent concentrations in
the waste or treatment residue of the waste do not
exceed the value shown in Table B for any hazardous
constituent listed in Table B for that waste..
(Source:
Amended at 16
Ill.
Reg.
,
effective
)
Section 728.142
Treatment Standards
expressed
as
Specified
Technologies
a)
The following wastes in subsections
(a) (1) and
(2) and
Table D and E must be treated using the
technology or
technologies specified in subsections
(a) (1) and
(2)
128—7 82
313
and Table
C.
1)
Liquid
hazardous
wastes
containing
PCBs
at
concentrations
greater
than
or
equal
to
50
ppm
but
less than 500 ppm must be incinerated in
accordance with technical requirements at 40 CFR
761.70, incorporated by reference in 35 Ill. Adm.
Code 720.111, or burned in high efficiency boilers
in accordance with the technical requirements of
40 CFR 761.60.
Liquid hazardous wastes
containing PCB5
at
concentrations
greater
than or
equal to 500 ppm must be incinerated in accordance
with the technical
requirements
of
40 CFR 761.70.
Thermal treatment in accordance with this Section
must be in compliance with applicable regulations
in 35 Ill. Adm. Code 724, 725 and 726.
2)
Nonliquid hazardous wastes containing halogenated
organic compounds
(HOC5)
in total concentrations
greater than or equal to 1000 mg/kg and liquid
HOC-containing wastes that are prohibited under
Section 728.132(e) (1) must be incinerated in
accordance with the requirements of 35 Ill.
Adm.
Code 724.Subpart 0 or 35 Ill. Adm. Code
725.Subpart 0.
These treatment standards do not
apply where the waste is subject to a Subpart £~
treatment standard for a specific HOC (such as a
hazardous
waste chlorinated solvent for which a
treatment
standard
is established under Section
728.141(a)).
fl
A mixture consisting of wastewater, the discharge
of which is subiect to regulation under 35 Ill.
Adm. Code 309 or
310..
and de minimis losses of
materials from manufacturing operations in which
these materials are used as raw materials or are
produced as products in the manufacturing process,
and that meet the criteria of the DOO1 ignitable
liguids containing areater than 10
total organic
constituents
(TOC)
subcategory.
is sublect to the
DEACT treatment standard described in Table
C.
For purposes of this subsection,
“de minimis
losses” include:
~j
Those from normal material handling
operations
(e.g..
spills from the unloading
or transfer of materials from bins or other
containers,
leaks from pipes,
valves or other
devices used to transfer materials)
~j.
Minor leaks from process equipment,
storage
tanks, or containers
128—783
314
Qj.
Leaks from well-maintained pump packinas and
seals
~j
Sample puraings; and
~J
Relief device discharges.
b)
Any person may submit an application to the Agency
demonstrating that an alternative treatment method can
achieve a level of performance equivalent to that
achievable by methods specified
in
subsections
(a),
(c
and
(d).
The applicant shall submit information
demonstrating that the applicant’s treatment method is
in compliance with federal and state requirements,
including this Part,
35
Ill.
Adm.
Code. 709,
724,
725,
726 and 729 and Sections 22.6 and 39(h)
of the
Environmental Protection Act
(Ill. Rev.
Stat.
1987, ch
111½,
pars.
1022.6 and 1039(h)), and is prOtective~.of
human health or the environment.
On the basis of such
information and any other available information, the
Agency shall approve the use of the alternative
treatment method if the Agency finds that the
alternative treatment method provides a measure of
performance equivalent to that achieved
by
methods
specified in subsections
(a),
(c) and
(d)..
Any
approval must be stated in writing and may contain suci
provisions and conditions as the Agency determines to
be appropriate.
The person to whom such approval is
issued shall comply with all limitations contained in
such determination.
c)
As an alternative to the otherwise applicable Subpart
I
treatment standards,
lab packs are eligible for land
disposal provided the following requirements are met:
1)
The lab packs comply with the applicable
provisions of 35
Ill.
Adm. Code 724.416 and
725.416;
BOARD NOTE:
35
Ill. Adm.
Code
729.301
and
729.31:
include additional restrictions on the use of lab
packs.
2)
All hazardous wastes contained in such lab packs
are specified in Appendix D or Appendix E;
3)
The lab packs are incinerated in accordance with
the requirements of 35 Ill.
Adin. Code 724.Subpart
0
or 35 Ill. Adm. Code 725.Subpart 0; and
4)
Any incinerator residues from lab packs containiru
128—784
315
DOO4,
D005, DOO6,
D007,
D008, DO1O and DOll are
treated in compliance with the applicable
treatment
standards
specified for such wastes
in
Subpart D.
d)
Radioactive hazardous mixed wastes
with
treatment
standards specified in Table E are not subject to any
treatment
standards
specified
in
Section
728.141,
Section
728.143
or
Table
D.
Radioactive
hazardous
mixed
wastes
not
subject
to
treatment
standards
in
Table E remain subject to all applicable treatment
standards
specified
in
Section
728.141,
Section
728.143
and
Table
D.
(Source:
Amended at 16 Ill.
Reg.
,
effective
Section 728.144
Adjustment of Treatment Standard
a)
Where the treatment standard is expressed as a
concentration in a waste or
waste
extract
and
a
waste
cannot be treated to the specified level,
or where the
treatment technology is not appropriate to the waste,
the generator or treatment facility may petition to the
Board for an adjusted treatment standard.
As
justification, the petitioner shall demonstrate that,
because the physical or chemical properties of.the
waste differ significantly from wastes analyzed in
developing the treatment standard, the waste cannot be
treated to specified level or by the specified methods.
b)
Each petition must be submitted
in
accordance
with the
procedures in 35 Ill.
Adin. Code l06.Sub~artG.
c)
Each petition must include the following statement
signed by the petitioner or an authorized
representative:
I certify under penalty of law that
I have
personally examined and am familiar with the
information
submitted
in
this
petition
and
all
attached documents,
and that, based on my ‘inquiry
of those individuals immediately responsible for
obtaining
the
information,
I
believe
that
the
submitted information is true,
accurate and
complete.
I
am
aware
that
there
are
significant
penalties
for
submitting
false
information,
including the possibility of fine and
imprisonment.
d)
After receiving a petition for adjustment of a
treatment standard, the Board may request any
128—785
316
additional information or samples which are necessary
to evaluate the petition.
e)
The Board will give public notice and provide an
opportunity for public comment, as provided in 35 Iii.
Adm. Code 106.
The final decision on an adjusted
treatment standard will be published in the
Environmental Rcgister.In conjunction with the normal
updating of the RCRA regulations, the Board will
maintain,
in this Part.
a listing of all adjusted
standards granted by the Board pursuant to this
Section.
A
LISTING
OF
ALL
ADJUSTED
STANDARDS
GRANTED
PURSUANT TO THIS SECTION WILL BE PUBLISHED
IN
THE
ILLINOIS REGISTER
AND
ENVIRONIENTAL
REGISTER AT THE
END
OF
EACH
FISCAL
YEAR.
(Section 28.1(d) (3)
of the
Environmental Protection Act.)
f)
A generator, treatment facility or disposal facility
that is managing a waste covered by an adjusted
treatment standard shall comply with the waste analysis
requirements for restricted wastes found under Section
728.107.
g)
During the petition review process, the applicant is
required tocomply with all restrictions on land
disposal under this Part once the effective date for
the waste has been reached.
h)
Where the treatment standard is expressed as a
concentration in a waste, or waste extract and a waste
generated under conditions specific to only one site
cannot be treated to the specified level, or where
treatment technology is not appropriate to the waste,
the generator or treatment facility may petition the
Board for a site-specific adjusted standard.
The
petitioner shall demonstrate that, because the physical
or chemical properties of the waste differs
significantly from the waste analyzed in developing the
treatment standard,
the waste cannot be treated to
specified levels or by the specified methods.
1)
Each petition for a site-specific adjusted standard
must include the information in 40
CFrt 260.20(b) (1)
through
(b) (4), ‘incorporated by reference in 35 111.
Adin.
Code 720.11135 Ill.
Adm. Code 720.120(b) (1)
—
(4).
j)
After receiving a petition for a site—specific adjusted
standard, the Board may request any additional
information or samples which the Board determines are
necessary to evaluate the application.
k)
A generator, treatment facility or disposal facility
128—786
317
which is managing a waste covered by a site—specific
adjusted standard from a treatment standard shall
comply with the waste analysis requirements for
restricted wastes in Section 728.107.
1)
During the petition review process, the petitioner for
a site-specific adjusted standard shall comply with all
restrictions on land disposal under this Part once the
effective date for the waste has been reached.
(Source:
Amended at 16 Ill. Reg.
,
effective
Section 728.Appendix D
Organometallic
Lab
Packs
Hazardous waste with the following EPA hazardous waste codes
numbers may be placed in an “organometallic” or “Appendix D lab
pack:”
POOl,
P015,
P027,
P040,
P002,
P016,
P028,
P041,
P003,
P017,
P029,
P004,
P018,
P030,
P005,
P020,
P031,
P044,
P006,
P021,,
P033,
P045,
P007,
P022,
P034,
P046.
P008,
P023,
P036,
P047,
P009,
P024,
P037,
P048,
P013,
r025,
P038,
P049,
P014,
P026,
P039,
P050,
P042, P043,
P051,
P066,
P054,
P067,
P056,
P068,
P057,
P069,
P058,
‘P070,
P059,
P071,
P060,
P072,
P062,
P073,
P063,
P074,
P064,
P075,
P065,
P077,
P081,
P082,
P084, P085,
P087,
P088,
P089,
P092, P093,
P094, P095,
P096,
P097,
P098, P099,
P101,
P102,
P103,
P104, P105,
P106,
P108,
P109,
P110,
P111. P112, P113,
P114,
P115,
P116, P118,
P119,
P120,
P121,
P122,
P123
13001, U002,
U003,
U004, U005,
U006,
U007,
13008,
U009,
U010,
U011,
13012,
13014,
13015,
U016,
13017,
U018,
U019, U020,
U021,
U022,
U023,
13024, U025,
13026, U027,
U028,
U029,
U030,
U031, U032,
U033,
U034,
U035, U036,
13037,
U038,
U039,
U041,
U042,
U043, U044,
U045,
13046,
U047, U048,
13049,
U050, U051,
13052,
U053, U055,
U056,
U057,
U058,
U059,
U060,
U061, U062,
13063, U064,
13066,
U067,
13068,
U069,
13070,
13071,
U0.72,
U073, U074,
13075,
13076,
U077,
U078, U079,
U080,
13081,
U082, U083,
U084,
13085,
U086,
U087,
U088, U089,
U090,
U091,
13092,
U093,
U094,
13095,
13096,
U097,
U098,
U099,
UlOl, U102,
U103,
13105,
U106, U107,
U108,
13109,
13110, U111,
U112,
U113, U114,
U115,
13116,
U117,
U128,
U118,
13129,
U119,
U130,
13120,
U131,
U121,
U132,
U122,
U133,
13123, U124,
U125,
13126,
13127,
13134,
U135, U136,
U137,
13136,
13137, Ul38,
U139, U140,
U141,
U142,
U143, U144,
U145,
U146,
U147,
U148, U149,
U150, U152,
13154,
U153,
U154, U155,
13156,
13157,
13158,
U159, U160,
U161, U162,
U163.
U164,
U165,
U166, U167,
U168,
13169,
U170, U171,
13172,
U173,
U174,
13176,
U177,
U178, U179,
U180,
13181,
13182, U183,
13184,
13185, U186,
13187,
U188,
U189, U190,
13191,
13192,
U193,
U194,
13196,
U197,
U200,
U201,
13202, U203, U204,
U205,
U206,
13207,
13208,
13209,
U210, U211,
U213,
13214,
13215, U216,
U217,
U218,
U219, U220,
13221,
U222,
13223,
13225, U226,
13227,
13228,
U234,
13235,
U236,
13237,
U238,
13239, U240,
13243, U244,
U246,
13247, U248, U249~
13323,
U353,
13359
128—787
318
DOOl,
D002, D003,
D004,
D005, D006,
D013,
D014, D015,
D016, DOll
D007, D008,
DOlO, Doll,
D012,
13032,
13136, U144,
13145,
13146, U163,
13214, U215,
13216,
13217
BOARD NOTE:
35
Ill. Adm. Code 729.301 and 729.312 include
additional limitations on the use of lab packs.
(Source:
Amended at 16
Ill. Reg.
effective
Section 728.Appendix E
Organic Lab Packs
Hazardous wastes with the following EPA Hazardous Waste Code No.
may be placed in an “organic” or “Appendix E” lab pack:
P001,
P002,
P015,
P016,
P027,
P028,
P041,
P042,
P054,
P057,
P067,
P068,
P082,
P084,
P097,
P098,
P110,
P111,
P123
P022,
P023,
P036,
P037,
P047,
P048,
P063,
P064,
P073,
P074,
P092,
P093,
P104,
P105,
-P116, P118~
P009, P013,
P014,
P025,
P024,
P026,
P033,
P039,
P040,
P049,
P050, P051,
P064,
P065,
P066,
—P075,
P077,
P081,
P094,
P095,
P096,
P106,
P108, P109,
P119,
P120,
P122,
FOOl,
F002,
F003,
F004,
F005,
F006,
FOlO, F020,
F021, F022,
F023,
F024,
F025 F026,
F027,
F028.
F039
1(001,
1(002,
1(008,
1(009,
1(010,
1(011,
1(013,
1(014,
1(015,
1(016,
K017,
1(018,
1(019,
1(020,
1(021,
1(022, K023,
1(024,
1(025,
1(026,
1(027,
1(028,
1(029,
1(030,
1(031,
1(032,
1(033,
1(034,
1(035,
1(036, K037,
1(038,
K039,
1(040,
1(051,
1(041,
1(052,
1(042,
1(054,
1(043,
1(060,
1(044,
1(061,
1(045,
1(046,
1(047, K048,
1(049,
1(050,
1(071,
1(073,
1(064,
1(065,
1(066,
1(069,
1(083,
K099,
1(084,
J’~1O1,
1(085,
1(102,
1(086,
1(103,
1(087,
1(104,
1(093,
1(105,
1(094,
1(095, K096,
K113,
1(097,1(098,
1(114,
1(115,
Kill,
1(112,
1(136
K116,
1(117,
KilO,
1(123,
1(124,
1(125,
1(126,
P003,
P004, P005, P006,
P007,
P008,
P017,
P018,
P020,
P030,
P031,
P033,
P043,
P044,
P045,
P058, P059,
P060,
P069,
P070,
P071,
P085,
P087,
P088,
P099,
P101,
P102,
P112,
P113,
P114,
P021,
P034,
P046,
P062,
P072,
P089,
P103,
P115,
UO06,
13018,
U029,
13042,
U053,
U066,
13077,
13088,.
U099,
13112,
13123,
U135,
13001,
13012,
13024,
13036,
13048,
13060,
13072,
13083,
13094,
13107,
U118,
13129,
13002,
U0l4,
U025,
U037,
U049,
U061,
13073,
13084,
13095,
13108,
U119,
U130,
13003,
U015,
13026,
13038,
13050,
13062,
U074,
U085,
U096,
13109,
U120,
U131,
13004,
U005,
13016,
U0l7,
13027,
U028,
U039,
13041,
U051,
13052,
13063,
U064,
U075,
13076,
13086,
U087,
13097,
13098,
13110,
13111,
13121,
13122,
13132,
U133,
U007,
13019,
U030,
13043,
13055,
U067,
U078,
U089,
UlOl,
13113,
U124,
13137,
U008,
U020,
13031,
13044,
U056,
U068,
U079,
13090,
U102,
U114,
13125,
13138,
U009,
U010,
13011,
U02l,
•U022,
U023,
13033,
13034, U035,
U045,
U046,
13047,
U057,
13058,
U059,
U069,
13070,
U071,
13080,
13081,
13082,
13091,
13092,
U093,
U103,
Ul05,
U106,
U115,
13116,
13117,
U126,
13127,
13128,
U139,
Ul40,
13141,
128—788
FOOl,
F002,
F003,
F004,
F005,
F025,
F026,
F027, F028
FOlO,
F020,
F021,
F022,
F023,
F024,
1(014,
1(025,
1(037,
1(040,
KilO,
1(017,
1(029,
1(040,
1(051,
-1(093,
1(105,
Ttl
~
1(018,
1(019,
1(030,
1(031,
1(041,
1(042,
1(052,
1(054,
1(094,
1(095,
Kill, ‘1(112,
1(12-6,
1(136
DOOl,
D0l2,
DO13,
D014,
D015,
DO16,
D017
BOARD NOTE:
35 Ill.
Adm.
Code 729.301 and 729.312 include
additional limitations on the use of lab packs.
(Sotirce:
Amended at 16 Ill. Reg.
)
,
effective
Section 728.Appendix G
The following are the effective dates for the USEPA rules
in 40
CFR 268.
These generally became effective as Illinois rules at a
later date.
Wa3te Code
Waste Category
Effective
date
California
list
Liquid
hazardous
wastes,
including
July
C,
1987
free
liquids
associated
with
solid
or sludge,
containing free cyanides
at concentrations greater than or
equal to 1,000 mg/i or certain
metals or compounds of these metals
~r~nt~
f~hnn
ni-
egual t~th~
California list
Liquid (aqueous)
having a pH less
-J-
July
0,
1937
319
U142,
13143,
13147, 13148,
U149,
13150,
13152, U153,
U154,
13155,
13156,
U157,
U158,
U159,
13160,
Ui61,
U162,
13163, U164,
U165,
13166,
13167,
13168,
U169,
U170,
U171,
13172, U173,
13174,
U176,
U177, U178,
13179,
U180,
13181,
U182,
13183, Ui84,
U185,
13186, U187,
13188, U189,
U190,
U191,
U192,
U193,
U194,
U196,’
13197,
U200,
U201,
13202,
13203,
13205,
13206,
U207,
U208,
13209,
13210, U211,
13213,
13214,
13218,
13219, U220,
13221,
U238,
13222,
13239,
U223,
U240,
13225,
13243,
13226,
U244,
U227,
U246,
U228,
U247,
U234,
U248,
U235,
13249,
13236,
13237,
13328, U353,
U359
1(001,
1(009,
1(010,
1(011,
1(013,
1(020,
1(021,
1(022,
1(023,
1(024,
1(032,
1(033,
1(034,
1(035,
1(036,
1(043,
1(044,
1(045,
1(046,
K047,
1(060,
1(065,
1(073,
1(033,
1(084,
K096,
1(097, K098,
1(099,
1(101,
1(113,
1(114,
1(115,
1(116,
1(117,
1(015,
1(016,
1(026,
1(027,
1(038,
1(039,
1(049,
1(050,
1(006,
1(087,
Federal Effective Dates
128—789
320
stewaters,
HOC
waste
mixtures
that
are
primarily
water
and that contain
greater than or equal to 1,000 mg/i
hut
1~
thnn
1flfl0fl
mn/I
California
list
Liquid
hazardous
waste
containing
PCBs greater than or equal
to
50
ppm
July
3,
1007
California
list
Other liquid and non liquid
hazardous wastes
containing
HOCs
in
total concentration greater than or
~nn~1
1r~
1flflfl
mr~
—
Nov.
3,
1080
California
list
C-all
DOOl
D002
D003
D004
Coil and debris HOCs not from
CERCLA/RCRA corrective actions
Coii and debris HOCs from
CEflCLA/RC1IA
corrective
actions
July
8,
1909
Nov.
8,
1900
Aug.
8,
1990
Aug.
8, 1090
Aug.
8,
1990
Nay
3,
1992
D004
D004
Wastcwater
Hay
3,
1992
Aug.
8,
1991
D005
DOO5
Inorganic solid debri~s
All others
DO06
D006
D~OO
7
DO07
D008
D003
Inorganic
solid
debris
All others
Inorganic solid debris
All others
Inorganic solid debris
Tr-,rl
ir~r~4
~oi~i
Hay
0,
1992
Aug.
3,
1900
May
0,
1092
Aug.
8,
1990
May 8,
1992
May
C,
D008
All others
128—
790
Aug.
8,
1990
California
list
~1efined as
July
Hay
8,
1992
———,~—
—,
321
May
0,
1~
May
-8,
1992
May 8, 199?
Aug.
0,
1990
High mercury nonwastewater
Low
mercury
nonwastewater
All others
Inorganic solid debris
Al-I others
Thorganic solid debris
All othera
A)~
Al~
Al~
A~
A~
M~
8,
1990
--—a
Aug.
May
Aug.
3,
1~90
BO~9
Deo~
~O~6
~GO1
F005
~0
01—P005
FGO1
P005
~FG02b
~OO5
C
~0O6
(cyanides)
exceot
Aug.
8,
1990
Aug.
8,
1-290
Aug.
0,
1990
Aug.
0,
1090
Aug.
8,
1990
Aug.
8
,
—,
Nov.
8,
1986
Nov.
8,
1900
Nov.
8,
1990
Aug.
8, 190O~
Aug.
8, 1990
Aug.
8, 1990
Aug.
3,
198-a
July
0,
1939-
All,
~
1isti..~,
Cmall
quantity
generators,
CEflCLA/RCflA
corrective action,
initial generator’s solvent water
mixtures, solvent containing
sludges and solids, and non
CEI1CLA/RCflA
corrective action soil3
with less than
1 percent total
solvent constituents
Coil and debris
A4~
Wastewater
128—79 1
322
P007
July 3,
1980
FOOB
P009
F-O
10
Polo
FOil
P012
Polo
P020
P020
D A ~
I
D A
I
‘Ji.
A
~.
~
r
‘J
r’
A
‘.
-~
£
~J.L.
F023
1’ A
I.
~
D A
~
I
‘J~.
r’f~
-~
I
~.Ii.
F024
(dioxi......,
P024
F025
FO 26
~
A
I
‘/~.
D A
‘~
I
~JL.
Coil and debris
All others
Coil and debris
All
others
Coil
and
debris
All others
Coil and debris
All others
Coil and debris
All others
Coil and debris
Nonwastewater
All others
Coil and debris
All
others
Coil
and
debris
July
8,
1-980
July
8,
1989
June 8,
1991
June 8,
1989
July
C,
1989
July 3,
1939
Aug.
C,
1990
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
3,
1988
June
8,
1991
Aug.
0,
1990
Aug.
3,
1990
June
8,
1939
Aug.
8,
1990
Nov.
8,
1990
Nov.
8,
Nov.
8,
-1990
.
••~--t’-
A
I
~.Ii.
All others
Nov.
3,
1988
128—792
Nov.
8,
1990
Nov.
8,
1988
Aug.
8, 1990
May.
8,
1992
Aug.
0,
1990
Aug.
8,
1990
Aug.
8,
1988
Aug.
8,
1990
Aug.
8,
1990
hug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1900
June 8,
1991
June 8,
1909
June 0, 1~91
June
C,
1989
Aug.
8,
1990
June
8,
1909
June 8,
1991
Aug.
3,
1990
June
8,
1989
1(013
Cnil
ind
~it~hri~
June 0,
1991
K014
Wastewater
128—793
Aug.
8,
1990
323
Coil
and
debris
All others
Wastewater
P023
A
I
P030
FO39
1(001
1(001
-(-icad/organics)
1(001
1(002
1(003
1(0-04
1(005 d
1(0-06
1(007 d
1(008
KO 09
1(009
1(010
1(010
1(011
1(011
1(011
1(013
1(013
Coil and debris
All others
Coil and debris
All others
Coil and debris
All others
Wastewater
Coil
and
debris
Wastewa-ter
324
1(014
Nonwastewater
1(014
Coil
and
debris
1(015
Wastcwater
1(01-5
Nonwastewater
1(0-16
Coil and debris
1(016
All others
1(017
Coil and dcbris
All others
Coil and dcbris
1(0-10
1(018-
1(019
1(019
1(020
1(020
1(021 e
K022~
V A ~
-~
I~U~.
£.
11A
1
I~’J
V A ~
U
V
A ~
I~U~.
V
A ~
U
V
A ~
U
1(025
e
1(026
1(027
V
A
‘~
£~U
£
1(023
All others
Coil and debri~
All others
Al~
Wastewater
Nonwastewater
Fnil
rir~ë~
tir’hri~
Coil and debris
All others
Coil
and
debris
All others
Coil and debris
All others
Coil and debris
June
8,
1991
Aug.
3,
1908
Aug.
8,
1990
Aug.
0,
1990
Aug.
8,
1983
Aug.
3,
1990
Aug.
3,
1900
Aug.
3,
190~3
Aug.
0,
1990
Aug.
6,
1988
Aug.
8,
1990
Aug.
8,
1988
Aug.
C,
1990
Aug.
3,
1990
Aug.
3,
1900
Aug.
C,
1090
June
8,
1901
June
0,
1089
Aug.
8,
1090
Aug.
8,
1088
Aug.
0,
1990
Aug.
8,
1990
June
0,
1991
June
8,
1909
June
6,
1991
128—7 94
1(0-20
1(028
1(020
1(02!)
1(029
1(030
1(030
1(031
1(03.
1(032
1(033
1(034
1(035
1(036 e
1(037
1(037
1(037
1(038
1(038
1(039
1(039
1(040
1(040
1(041
VA
.4
—1
£~
U
T
1(043
All others
Wastewater
Nonwastcwat
Coil and debris
Coil and debris
All others
Wastewater
All
feil and debris
Wastewater
All
others
Coil
and
debris
All
others
Coil and debris
All others
~43
.~.ddebri..
All others
Al-a:
Al-a:
Coil and dcbri-s
+~
-~
—
June
8, 19?
Aug.
8,
190
June
B,
10~
June
8,
199
Aug.
0,
199
Aug.
8,
190
Aug.
8,
199-
May 8,
1992
‘Aug.
8, —199
Aug.
8,
199
Aug.
6,
109~
Aug.
Aug.
8,
0,
~4
~l
Aug.
8,
199(
Aug.
8,
l99(
Aug.
8, 19O~
June 8,
199
June 0, 196~
June
0,
1901
June 8,
1989
June
C,
1991
June
0,
1989
Aug.
3,
1930
Aug.
-8-7- -1990
June 8,
1
325
Aug.
8,
~
128—795
1(043
All
others
326
June
0,
1909
1(044
Al-I
1(045
Al-I
1(046
Al-I
Wastewater
Nonwastewater
Al-I
Al-I
Wastewater
1(034
1(035
Aug.
8,
1990
All others
Al-I
Wastewater
V.
~.‘z
in
.a
.~ t.~
V’
‘a
....Ca.
Wastewater
Wastewater
Wastewater
K046
1(047
1(040
1(043
1(049
1(049
1(050
1(050
1(051
1(051
1(052
Wastewater
1(052
1(060
1(061
1(061
1(062
1(069
1(073
1(083
1(084
Aug.
~i,
iiu
Aug.
8,
1990
Aug.
8,
1900
Aug.
3,
1990
Aug.
0,
1990
Aug.
0,
1990
Nov.
8,
1990
Aug.
0,
1990
Nov.
8,
1990
Aug.
8,
1990
Nov.
8,
1990
Aug.
8,
1990
Nov.
0,
1990
Aug.
8,
1990
Nov.
3,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
0,
1903
Aug.
-8-7 1980
Aug.
8,
1990
Aug.
-8-7- 1990
Aug.
0,
1990
Aug.
-8-i 1990
May
3,
1092
128—7
96
327
Aug.
8,
1000
Aug.
8,
1990
Aug.
8,
1988
June C,
199.
June 8,
1909
June
8.,
1991
June 8,
1989
Aug.
8,
1990
June 0,
1939
June 3,
1001
Aug.
8,
1990
June 0,
1089
June 8,
1991
Aug..
C,
1090
Aug.
0,
1990
Aug.
8,
1988
Aug.
8,
1990
Aug.
0,
1903
May 0,
1992
Aug.
8,
1990
Aug.
8,
1980
Aug.
8,
1990
1(104
1(105
All others
Al-I
128—79
7
Aug.
8,
1908
Aug.
C,
1990
Coil and debris
All others
Nonwastewater
F!r~i1
r~n,-1
i~r~hvi~z
1(086
1(087
1(087
1(093
Al-I
Coil and ~
1(093
All others
1(094
1(094
Coil and debris
All
others
1(095
Wastewater
1(095
1(095
--
1(096
Wastcwater
1(096
1(096
Nonwastewater
Coil and debris
1(097
Al-I
1(093
Al-I
1(099
Al-I
1(100 e
Al-I
1(101
1(101
1(102
1(102
1(103
1(103
Wastcwater
Nonwas’-~”-~--
Wastewater
Nonwastew&~
Coil and debris
All others
1(104
Coil and debris
May 0,
1992
———‘~—
—I
1(106
1(106
1(106
1(113
1(113
1(114
1(114
1(115
1(115
1(116
1(116
POOl
P002
P003
P004
P005
ro
06
P007
P008
P009
Coil
and
debris
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Coil
and
debris
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Al-I
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May 0,
1992
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C,
1992
AUG.
June
U,
8,
1JJ0
1991
June 8,
1980
June 8,
1991
June 3,
198-9
June 8,
1991
June C,
198-9
June C,
199-1
June
8,
196-9
Aug.
3,
1990
Aug.
8,
199-0
Aug.
3,
1990
Aug.
8,
1990
Aug.
0,
1990
Aug.
8,
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0,
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Aug.
3,
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0,
1990
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Hay 8,
1992
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0,
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0,
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May
8,
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328
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mercury
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nrnwtewater
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Coil and debris
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r.A1
~
£
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Wastewatcr
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128—798
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Al-I
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Nonwastewater
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Coil and debris
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Aug.
C,
Aug.
0,
199
Aug.
8,
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8,
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1991
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9
329
128—799
P040
P040
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P041
Coil
and
debris
P041
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others
P042
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P043
Coil ana acoris
P043
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P044
Coil
and
debris
P044
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P045
Al-I
P046
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P047
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P043
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P049
Al-I
P050
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P051
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P056
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P062
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330
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8,
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8,
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June
8,
1991
June
C,
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June
8,
1991
June
3,
1989
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Aug.
0,
1990
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3,
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Aug.
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1990
Aug.
8,
1990
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8,
1990
Aug.
8,
1990
Aug.
3,
1990
Aug.
3,
1990
Aug.
8,
1990
Aug.
0,
1990
Aug.
0,
1990
June 8,
1091
June
3,
1909
June 8,
1939
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3,
1990
All
others
All-
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P065
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331
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All
Al-I
May 0,
1992
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1992
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0,
1990
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others
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All-
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All-
All
Al-I
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June
0,
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June
8,
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Aug.
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1990
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8,
1990
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1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
3,
1990
Aug.
3,
1990
Aug.
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1990
June
8,
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June
0,
1939
Coil and debris
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All
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fr)il
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May 8,
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0,
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0,
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128—801
May
8,
1992
Nay 8,
1992
Aug.
0,
1990
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1992
Aug.
8,
1990
June
3,
1991
May
0,
1992
Aug.
3,
1990
Aug.
3,
1990
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1991
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1939
June 0,
1909
Aug.
8,
1990
June 0,
1909
June
3,
1989
Aug.
8,
1990
Aug.
8,
1990
Aug.
3,
1990
Aug.
0,
1990
June C,
1009
June
C,
1989
Aug.
8,
1990
June 3,
1909
332
High
mercury
nonwastewater
T.~t..i
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P093
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P094
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——
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Coil and debris
All
others
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All others
Coil
and
debris
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Al-I
P096
P097
Coil and debris
P097
All others
P098
Al-I
P099
(silver)
P099
(cyanides)
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P099
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P101
All
P102
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Coil and debris
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Al-I
Al-I
All
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Coil and debris
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Coil and debris
All others
Aug.
8,
1990
May
8,
1992
Aug.
8,
1990
Aug.
8,
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All
Aug.
8,
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333
May 8,
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June
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June
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Aug.
8,
1990
Aug.
8,
1990
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8,
1990
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1992
Aug.
8,
1990
MayO,
1992
Aug.
8,
1990
P119
P120
All-
Al-I
Al-I
Al-I
All
All-
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Aug.
8,
1990
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3,
1990
June
C,
1989
Aug.
0,
1990
Aug.
0,
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Aug.
0,
1990
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May 8,
1992
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1992
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3,
1990
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3,
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May
8,
1992
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1990
334
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All others
A-Il
All
Coil
and
debris
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Coil and debris
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Al-I
Coil
and
debris
All
others
Coil and debris
All others
A-Il
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U006
Up 07
U007
U008
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All
Al-I
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.——,~.
~,
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B,
1990
All
others
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and
debris
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A-Il
All
128—804
13024
U025
U026
U0 26
UP 27
U020
13028
U0 29
Aug.
8,
1990
Aug.
8,
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Aug.
8,
1990
May
8,
1992
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C,
1990
May
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1992
13034
All others
Aug.
8,
1990
U035
Coil and debris
May 8,
1992
U035
All others
Aug.
C,
1990
U036
A-Il
13037
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May 0,
1992
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1990
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1992
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8,
1990
335
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0,
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Coil and debris
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All
All
All
Al-I
Coil and debris
All
others
Coil
and
debris
June
0,
1989
13030
13031
13032
U033
U033
U034
..—.~.
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Aug.
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U033
U0 33
13039
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Coil
All
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and
debris
others
and debris
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1
T”~
All
others
128—805
336
U043
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All
All
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Coil and debris
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others
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~flU
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~IA1I
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1900
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1990
May 3,
1992
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3,
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8,. 1990
C,
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Aug.
0,
1000
Aug.
8,
1900
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3,
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0,
1990
Aug.
8,
1990
Aug.
C,
1900
Aug.
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1000
Aug.
3,
1990
June
3,
1992
June
C,
1989
Nay
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1002
Aug.
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1900
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1900
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128—806
337
13063
All
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1989
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13073
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All others
All
All
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All
All
Nay
3,
1992
Aug.
3,
1000
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1000
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8,
1000
Aug.
0,
1900
Aug.
8,
1000
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8,
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8,
1900
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0,
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8,
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13064
U066
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All
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0,
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0,
1900
Aug.
8,
1000
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Aug.
13071
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Aug.
8,
1090
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128—807
338
June
6,
1-9-8-9
June
8,
19-9-1
June
3,
1030
Aug.
3,
1990
Aug.
8,
1990
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1092
Aug.
3,
1090
May
8,
1992
Aug.
6, l9~Q
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3,
1992
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8,
1900
Aug.
C,
1990
Hay
3,
1092
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8,
1900
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3,
1000
Nay
8,
1992
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
June
8,
1901
June
6-,
1989
Aug.
13,
1990
Aug.
3-,
1990
Aug.
8,
1900
Coil and debris
All others
Soil and debrL,
All
others
All
All
“.c~i1
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13087
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13098
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13103
13106
All
others
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and debris
All
others
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All
others
All
Soil and debris
All
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All
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others
All
All
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Coil and debris
All other-s
All
All
All
128—808
Ui07
339
June 8, l9~l
Ui07
13103
All
others
All
June
8,
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Aug.
8,
1990
U113
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All
Soil
and
debris
Aug.
8,
1090
Hay
3,
1002
Aug.
3,
1990
Aug.
3,
1990
Aug.
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1090
Aug.
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3,
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3,
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Aug.
3,
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3,
1-990
Aug.
C,
1900
Aug.
8,
1090
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1990
13124
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~
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Aug.
3,
19~’~~•-
13109
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All-
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UllO
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Ulil
All
U1l2
All
U114
All others
Ul15
13116
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Ui17
13118
Ui19
All
Coil and debris
All others
All
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nt~~~41
~-~-1
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U120
All
13121
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13126
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Aug.
3,
1090
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Coil and debris
All others
All
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others
All
All
All
Wastewater
Nonwastcwater
All
All
All
All
All
Soil and debris
All
others
All
All
Aug.
0,
LJJU
May
3,
1992
Aug.
8,
1990
Aug.
0,
1090
Nay 0,
1092
Aug.
0,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
3,
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Aug.
3,
1990
Nay
0,
1992
Aug.
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1900
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Aug.
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3,
1990
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1990
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3,
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Ul47
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All
All
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Soil and debris
Aug.
8,
1990
Aug.
0,
19-9-~
May
3,
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Aug.
0,
1990
Nay
C,
1902
340
Aug.
0,
1090
128—810
13140
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13151
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13153
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Ui 56
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Ui 60
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13163
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All others
Coil and debri-s-
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Coil and debris
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All
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All
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c~?-~ii
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All
All
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May
8,
1902
Aug.
6,
1900
Aug.
3,
1990
Aug.
3,
1990
341
Aug.
3,
1090
...—.z
~,
High mercury nonwastewater
Low mercury nonwastewater
Aug.
8,
1990
May
8,
1992
Hay 3,
1902
May 3,
1992
Aug.
3,
1090
Aug.
8,
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Aug.
3,
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Aug.
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May
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Aug.
8,
1000
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1000
Aug.
8,
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Aug.
3,
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Aug.
8,
i090
Aug.
8,
1990
May
8,
1992
Aug.
3,
1090
UiC4
13164
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Soil and debris
All others
All
All
128—811
Ul 67
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UI6C
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13170
Ul71
13171
13172
13173
13173
U174
13176
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Ul77
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Ui70
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13181
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S-e-ii
and debris
All
others
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Coil and debris
All others
All-
Coil and debris
All others
All
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All others
Soil and debris
All others
Soil and debris
All others
All
All
All
All
All
May
8,
1092
Aug.
8,
1090
Nay
8,
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Aug.
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1990
Aug.
8,
1990
Aug.
8,
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~
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1002
Aug.
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1030
Aug.
8,
1990
Nay 3,
1992
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Aug.
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1900
Hay
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Nay
Aug.
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1090
May
3,
Aug.
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1900
Aug.
8,
1090
Aug.
C,
1990
Aug.
8,
1990
May
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Aug.
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1990
Aug.
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342
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1990
All others
All
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11101
All
All
All
All
Soil
and
343
All others
Coil and debris
All others
Aug.
0,
19~~/
U-
~
Aug.
0,
1990
13-1-9-2
13193
Ul93
All
Soil and debris
All others
A~.
May
8,
l09-Z
Aug.
C,
1990
-------
F~. ~99~j
U203
13204
Nay
C, 1092
Aug.
8,
1990
Aug.
3,
19O~
Aug.
8,
1990
May
8,
1092
Aug.
8,
1900
Aug.
8,
1990
Nay
8,
1992
Aug.
8,
i990
U205
U2OC
All-
Coil and debris
—
1
Nay 8,
1992
TTA
LI
i.
LI
j
All others
All
Aug.
8,
i91i30
Aug.
3,
1090
Aug.
8,
1990
June
0,
1991
June
3,
1989
May
8,
1092
Aug.
8,
1990
13194
13194
13106
Ui97
T~TA
LI ~
11200
13201
TTA (~
A
LI ~
U
hA
A
LI
i.
Ui.
Soil and debris
All
others
All
All
Soil and debris
All
other-s
All
Soil and debris
All others
All
All
Aug.
8,
1300
Aug.
8,
1990
128—813
344
U209
11210
13211
TTA
LI
U2 14
hA
L’
i.
U218
U2l0
13210
IT A A
LI
TIA
A
LI
i.
hA
A
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£.
T~AA A
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TIA
A
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A
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U
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C.
TTA A
LIt.
i.
hA
A
LI
C.
C.
All others
Coil and debris
All others
All
Au;.
8,
1990
May 8,
1992
Aug.
0,
1990
Aug.
8,
1990
13234
All others
128—814
..—-~-
~,
13208
Aug.
8,
1900
All
All-
All
All-
All
All
All
All-
All-
U2i5
11216
..—.~.
—,
Aug.
8,
1990
Aug.—8-7
U2l8
AU~.
U,
.LJ~.JU
Aug.
3,
1990
Aug.
8,
1990
Aug.
3,
1990
Aug.
8,
1900
Nay
C,
1992
Soil and debris
June
8,
100.
May 6,
10-92
Aug.
3,
1000
June
C,
1991
All
Soil
others
and debris
All others
Soil and debris
All others
All
All
All
All
‘~r~i1~n~9
~hri~
hA
LI
C.
Aug.
3,
1090
Aug.
0,
1990
Aug.
8,
1990
Nay
8,
1992
345
ITA
LI
C.
C.—..
~
1
._.__:~
~
June
8,
1091
Nay
8,
1992
Aug.
3,
1990
Hay
3,
1992
13237
13238
U238
13239
13-240
All others
Coil and debris
All others
All-
Coil and debris
Aug.
3,
1900
May
3,
1902
Aug.
C,
1090
Aug.
3,
199-0
May
3,
1002
U240
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A
A
U
C.
~.)
U244
hA
LI
C.
All others
Aug.
3,
1090
U24G
All
Aug.
3,
109-0
U247
Al-I
13248
All
U249
All
AU~.
U,
.LJ~JU
Aug.
3,
1990
Aug.
8,
1090
-?--
This table does not include mixed radioactive wastc3
irom
the First,
Second,
and Third Third rules) which are
receiving
a national capacity variance until May 3,
1992 for
all applicable treatment technologies.
Standards arc being promulgated for 1,i,2 trichloroethanc
and 2
nitropropane for wastewaters and nonwastcwatcrs.
Ctandards arc being promulgated for benzene and
~ethoxycthanol
for wastewaters and nonwastewatcrs.
Treatment standards for nonwastewaters disposed of after
June
3,
1939,
were
promulgated
June
8,
1989.
Treatment standards for nonwastewaters disposed of after
Aw~st 17,
1030,
wer-& ~
ITA
A
C
U
C..)
U236
13236
ITA
Ut.
Au
others
Soil and debris
All others
Coil and debris
All
Soil
and debris
All other-s
Aug.
3,
1990
May
C,
1992
“—-:,.
~-‘
PA1~fAThl 1
Igated May
2,
128—815
346
TABLE
I
EFFECTIVE DATES OF SURFACE DISPOSED WASTES
(WON-SOIL AND DEBRIS) REGULATED IN THE LDRS
(A)
CONPREHENSIVE LIST
Waste code
Waste
category
Effective date
California list
California list
California
List
California
list
California list
0001
D002
0003
0004
0004
0005
0006
D007
D008
0008
0009
0009
0010
Doll
DOl2
0013
D014
DOl 5
0016
0017
FOOl
FOOl
F002 (1,1.2-
trichloroethane)
F002
F002
F003
F003
F004
F004
F005 (benzene,
2-ethoxy
ethanol,
2-
Liquid hazardous wastes,
including free liquids associated with solid
or sludge. containing free cyanides at concentrations greater than or
equal to 1.000 mg/I or certain metals or conpo4.mds of these metals
greater than or equaL to the prohibition levels
Liquid (aqueous) hazardous wastes having a PH Less than or equal to 2
Dilute HOC wastewaters, defined as HOC-waste mixtures that are
primarily water and that contain greater than or equal
to 1,000 mg /1
but less than 10.000 mg/I
Liquid hazardous waste containing PCB5 greater than or equal
to 50 ppm
Other liquid and nontiquid hazardous wastes containing HOCs
in total
concentration greater than or equal to 1.000 mg
Alt
All
All
Wastewater
Nonwastewater
All
ALL
All
Lead materials before secondary smelting
All others
Nonwastewater
All others
All
AtI
All
All
Alt
All
ALL
Small quantity generators. CERCLA response/RCRA corrective action.
initial generator’s solvent-water mixtures, solvent-containing sludges
and solids
All others
Wastewater and Nonwastewater
Small quantity generators, CERCIA response/RCRA corrective action.
initial generator’s solvent-water mixtures, solvent-containing sludges
and solids
All others
Small quantity generators, CERCLA response/RCRA corrective action.
initial generator’s solvent-water mixtures,
solvent-containing sludges
and solids
All others
Smell quantity generators. CERCLA response/RCRA corrective action,
initial generator’s solvent-water mixtures, solvent-containing sludges
and solids
All others
Wastewater and Nonwastewater
July 8. 1987.
July 8.
1987.
July 8,
1987.
July 8.
1987.
Nov. 8.
1988.
Aug. 8.
1990.
Aug. 8,
1990.
Aug. 8.
1990.
Aug. 8.
1990.
May 8.
1992.
Aug. 8.
1990.
Aug. 8.
1990.
Aug. 8,
1990.
May 8.
1992.
Aug. 8,
1990.
May 8.
1992.
Aug. 8,
1990.
Aug. 8,
1990.
Aug.
8. 1990.
Aug. 8.
1990.
Aug. 8.
1990.
Aug. 8. 1990~
Aug. 8. 1990.
Aug. 8.
1990.
Aug. 8.
1990.
Nov. 8. 1988.
Nov. 8. 1986.
Aug. 8.
1990.
Nov. 8.
1988.
Nov.
8. 1986.
Nov. 8.
1988.
Nov.
8.
1986.
Nov. 8.
1988.
Nov. 8,
1986.
Aug. 8,
1990.
128—816
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IP
355
1.
Sotvent-(F001-F005) and dioxin-(F020-F023 and
Nov.
8. 1990.
F026-F028) containing soil and debris from
CERCLA response of RCRA corrective actions.
2.
Soil and debris not from CERCLA response or
Nov. 8.
1988.
RCRA
corrective
actions contaminated with
Less than 1
totaL
solvents
(F001-F005) or
dioxins (F020-F023 and F026-F028).
3.
Soil and debris contaminated with
California
Nov.
8.
199~).
List HOCs from CERCLA response or RCRA
corrective
actions.
4.
Soil and debris contaminated with California
July 8.
1989.
List
HOCS
not from CERCLA response or RCRA
corrective actions.
ALL soiL and
debris
contaminated with First
Aug. 8.
1990.
Third wastes for which treatment standards
are
based on incineration.
6.
ALL
soil
and
debris
contaminated
with Second
Ji.tie 8.
1991.
Third
wastes
for
which
treatment standards
are
based
on
incineration.
ALL
soil
and debris contaminated with Third
Nay 8. 1992.
Third wastes
or.
First
or Second Third ttsoft
hemmert’
wastes
which
had
treatment
standards
proautgated
in
the
Third
Third
rule,
for
which
treatment standards are
based
on
incineration,
vitrification,
or
mercury
retorting,
acid leaching followed by chemical
precipitation, or
thermal recovery of metals.
as well
as all
inorganic solids
debris
contaminated with 0004-DOll wastes, and alt
soil and debris contaminated with mixed
RCRA/radioactive wastes.
BOARD NOTE: This table is
provided
for the convenience of the
reader.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
)
Section
728.Appendix
H
National
Capacity
LDR
Variances
for
UIC
Wastes
Wa3tc Code
w~i~c~ucegory
Effective
date
FOOl F005
All 3pent FOOl-F005 aolvent
Augu3t
C,
containing
less than
1 percent
1090
005
30
128—825
356
California list
(~r~’Iifnrr~in
1i’~*t~
Liquid hazardous wastes,
including
August
1990
C,
free liquids associated with any
solid or sludge, containing free
cyanides at concentrations greater
than or equal to 1,000 mg/i,
or
containing certain mctals or
August 8,
compounds of these metals greater
than or equal to the prohibition
levels
Liquid hazardous waste having a pH
1ia.~
-t-hrrn
ru-
a.rninl
jg’~ ~
1990
California list
hazardous wastes containing IlOCs in August
C,
total concentrations less than
1990
10,000 mg/i but greater than or
equal to 1,000 mg/i
D002 b
D003
(cyanides)
D003
(aulfides)
DO 03
(explosives,
react
ives)
May 8,
1902
Nay 8,
1902
May 8,
1092
June
8,
1991
May C,
1992
June C,
1991
KO11
June 0,
1991
KOll
K013
Wastewater
May 8,
1902
June C.
1091
K013
K014
Wastewater
May 3,
1992
May 0,
1992
June 3,
1991
A-I-):
A-I-):
May C,
1992
Nay 3,
1902
May
8,
1992
May
8,
1992
D007
D000
D009
Foil
FO30
KO09
High
Mcrcury
Nonwastewater
Low
Mercury Nonwastcwater
Wastewater
Wastewater
KO1C
(dilute)
128—826
357
KO4C
KO49
KO50
K05.
K052
KO62
K071
KI04
W;~t~-
six
rn
1900.
A-I-):
A-I-):
A-I-):
A-I-):
,,
as
August C,
1990
Augu3t 0,
1990
August 8,
1990
August
C,
1990
August
8,
1990
August
0,
1990
August
8,
1990
Auguat
C,
1990
Dccpweli injec
meet the Calif
1990.
D002 iiquid~with a pH lee
than
2
mus
I
Waste code
Waste category
Effective
date
FOOl—F005
California list
California list
All spent F001-F005 solvent
containing less than
1 percent
total F00i-F005 solvent
constituents
Liquid hazardous wastes,
including
free liquids associated with any
solid or sludae. containing free
cyanj.des at concentrations greater
than or equal to 1,000
maIl,
or
containing certain metals or
compounds of these metals areater
than or equal to the prohibition
levels
Liquid hazardous waste having a PH
less than or equal to 2
Hazardous wastes containing HOCs in
total concentrations less than
Aug.
8,
1990.
Aug.
8,
1990
Aug.
8,
1990.
Aug.
8,
1990.
California
list
128—827
358
D002 B
D003
(cyanidesi
D003
(sulfides)
D003
(explosives,
reactives).
D007
D009
F007
FO 39
KO09
KO11
KO11
KO13
KO13
KO14
K016
(dilute)
K049
K050
K051
KO52
KO 62
K07 1
KI04
All
All
All
All
Nonwastewater
All
Wastewater
Wastewater
Nonwastewater
Wastewater
Nonwastewater
Wastewater
All
All
All
All
All
All
All
All
All
1992.
1992.
1992.
1 qq2.
May 8,
1992.
MaY 8,
1992.
June 8,
1991.
May 8,
1992.
June 8.
1991.
June 8,
1991.
May 8.
1992.
June 8.
1991.
May
8,
1992.
May 8,
1992.
June 8,
1991.
Aug.
8,
1990.
Aug.
8.
1990.
Aug.
8,
1990.
Aug.
8.
1990.
Aug.
8,
1990.
Aug.
8,
1990.
Aug.
8,
1990.
Wastes that are deep well disposed on—site receive a six—
month
variance,
with
restrictions
effective
in
November
1990.
B
Dee~welliniected D002 liquids with a PH less than
2 must
meet the California List treatment standards on August 8,
1990.
BOARD NOTE:
This table is provided for the convenience of the
reader.
(Source:
Amended
at
16
Ill.
Reg.
,
effective
10,000 mg/i but greater than or
eaual to 1,000 m~/l
May 8.
May 8.
May 8.
M~v R.
128—8 28
359
)
Section 728.Arrnendix
I
EP Toxicity Test Method and Structural
Integrity Test
The Board incorporates by reference 40 CFR 268, Appendix IX,
adopted at 56 Fed. Req.
3876, January 31,
1991.
This Section
incorporates no future amendments or editions.
(Sourcç:
Added at 16 Ill.
Reg.
,
effective
)
Section 728.Table A Constituent Concentrations in Waste Extract
(CCWE)
0,
F and K Listed Wastes
CAS
Ho. for
Concentration
ReguLated
Concentration
(mglL)
Nonwaste-
Waste
See
ALso
Regulated
Hazardous Constituent
Hazardous
(mg/L)
Waste-
waters
Code
Constituent
waters
D004
Table
B
Arsenic
7440-38-2
NA
5.0
#A
D005
Table
B
Bariun
7440-39-3
NA
100.
0006
TabLe
B
Cackniun
7440-43-9
WA
1.0
0007
Table
B
Chromiijn (Total)
7440-47-32
HA
5.0
0008
Table B
Lead
7439-92-1
NA
5.0
ft~
0009 (Low Mercury Subcategory-
-
Less
than
260
rrv~/kg
Mercury)
TabLes
B
&
Mercury
7439-97-6
NA
0.20
0
0010
Table
B
Seleniun
7782-49-2
NA
5.7
0011
TabLe
B
Silver
7440-22-4
NA
5.0
FO01-F005
spent
solvents
Tables
B
&
Acetone
67-64-1
0.2~O5
0.59
0
n-ButyL aLcohoL
71-36-3
5.0
5.0
Carbon disuLfide
75-15-0
1.05
4.81
Carbon tetrachtoride
56-23-5
005
O•96
Chtorobenzene
108-90-7
0.15
0.05
Cresols
(and
cresyLic
acid)
2.82
0.75
Cyctohexanone
108-94-1
0.125
0.75
1,2-DichLorobenzene
95-50-1
0.65
0.125
Ethyl
acetate
141-78-6
0.05
0.75
Ethytbenzene
100-41 -4
0.05
0.053
EthyL
ether
60-29-7
0.05
0.75
Isobutanol
78-83-1
5.0
5.0
MethanoL
67-56-1
0.25
0.75
Methytene
chloride
75-9-2
0.20
0.996
Methyl
ethyL
ketone
78-93-3
0.05
0.75
MethyL
isobutyL
ketone
108-10-1
0.05
0.33
Nitrobenzene
98-95-3
0.66
0.125
Pyridine
110-86-1
1.12
0.33
Tetrachloroethylene
127-18-4
0.079
-0.05
128—829
360
F0l9
Table
B
Chromiun (Total)
108-88-3
71-55-6
76-13-1
79-01-6
75-69-4
7440~43-9
7440-47-32
7439-92-1
7440-02-0
7440-22-4
7440-43-9
7440-47-32
7439-92-1
7440-02-0
7440-22-4
7440-43-9
7440-47-32
7439-92-1
7440-02-0
7440-22-4
7440-43-9
7440-47-32
7439-92-1
7440-02-0
7440-22-4
7440-47-32
1.12
1.05
1.05
0.062
0.05
0.05
NA
NA
HA
NA
NA
NA
NA
NA
NA
NA
NA
HA
NA
NA
NA
NA
NA
NA
NA
NA
NA
0.47~
0.33
0.41
0.96
0.091
0.96
0.15
0.066
5.2
0.51
0.32
0.072
0.066
52
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
5.2
F024
Table B
Chroiniun
(Total)
NA
Totuene
1, 1, 1-Trichtoroethane
1,1,2-Trichtoro-i,2,2-trifluoro-
ethane
Trichloroethylene
TrichloroiLuoromethane
Xytene
F006
Table B
Caóniui~
Chromiun (Total)
Lead
Nickel
Silver
F007
Table B
Caäniun
Chromiun (Total)
Lead
Nickel
Silver
F008
Table
8
Cadnii.xn
Chromiun
(Total)
Lead
Nickel
Silver
F009
Table
B
Cadeiun
Chroiniun (Total)
Lead
Nickel
Silver
FOIl
Table B
Caciniun
Chromiun (Total)
Lead
Nickel
Silver
F012
Table
B
Cathiun
Chromiun (Total)
Lead
Nickel
Silver
7440-43-9
NA
0.066
7440-47-32
NA
5.2
7439-92-1
NA
0.51
7440-02-0
NA
0.32
7440-22-4
NA
0.072
7440-43-9
NA
0.066
7440-47-32
NA
5.2
7439-92-1
NA
0.51
7440-02-0
NA
0.32
7440-22-4
NA
0.072
F020-F023 and
F026-F028 dioxin-containing
wastes
*
B
HxcDD-AlL
Hexachlorodibenzo-p-
dicxins
HxcDF-ALl
Hexachlorodibenzofurans
PeCDD-ALL
Pentachlorodibenzo-p-
di ox
ins
PecDF-ALI
Pentachtorodibenzofurans
TCDD-ALI
Tetrachlorodibenzo-p-
di ox
ins
TcDF-AIL
Tetrachtorodibenzofurans
2,4,5-Trichlorophenot
2,4,6-TrichLorophenol
2,3,4,6-TetrachLorophenol
PentachtoraphenoL
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
l
ppb
-ci.
ppb
ci.
ppb
-ci.
ppb
1.
ppb
-‘1.
ppb
0.0k p~~
~
0.05
ppm
0.05
ppm
0.0~Qj
1.
ppb
—0.05 ppm
~.L.
~
0.05
ppm
0.05
ppm
0.05.Qj.
95-95-4
88-06-2
58-90-2
87-86-5
7440-47-32
ppm
ppm
0.0Th
128—830
361
Lead
7439-92-1
NA
0-.~24Reserv’
Nickel
7440-02-0
NA
0.088
F039
Table B
Antimony
7440-36-0
NA
0.23
Arsenic
7440-38-2
NA
5.0
Bariun
7440-39-3
NA
52.
CacIniun
7440-43-9
NA
0.066
Chrouniun
(Total)
7440-47-32
HA
5.2
Lead
7439-92-i
NA
0.51
Mercury
7439-97-6
NA
0.025
NickeL
7440-02-0
MA
0.32
Seleniuii
7782-49-2
NA
5.7
Silver
7440-22-4
NA
0.072
KOOl
Table B
Lead
7439-92-1
NA
0.51
K002
Table
B
Chromiun
(TotaL)
7440-47-32
NA
0.094
Lead
7439-92-i
NA
0.37
K003
Table 8
Chromiun (Total)
7440-47-32
NA
0.094
Lead
7439-92-1
NA
0.37
K004
Table B
Chroniiun (Total)
7440-47-32
NA
0.094
Lead
7439-92-i
WA
0.37
K005
Table
B
Chromiun
(Total)
7440-47-32
NA
0.094
Lead
7439-92-i
NA
0.37
K006
Table B
Chromiun
(Total)
7440-47-32
NA
0.094
(anhy-
drous)
Lead
7439-92-1
NA
0.37
1(006
Table
B
Chromiun
(TotaL)
7440-47-32
NA
5.2
(hy-
drated)
K007
Table B
Chromiun (Total)
7440-47-32
NA
0.094
Lead
7439-92-1
NA
0.37
1(008
Table B
Chromiun (Total)
7440-47-32
HA
0.094
Lead
7439-92-1
WA
0.37
1(015
Table
B
Chromiun (Total)
7440-47-32
NA
1.7
71~39-92-1
NA
0.2
Nickel
7440-02-0
1(021
Table
B
Antimony
7440-36-0
NA
0.23 #
1(022
TabLe
B
Chromiun
(Total)
7440-47-32
WA
5.2
Nickel
7440-02-4-0
NA
0.32
1(028
Table 8
Chromiun (Total)
7440-47-32
NA
0.073
Lead
7439-92-i
NA
0.021
Nickel
7440-024-0
NA
0.088
1(031
TabLe
B
Arsenic
7440-38-2
NA
5.6 #
A
1(046
TabLe B
Lead
7439-92-1
NA
0.18
1(048
Table B
Chromiun (Total)
7460-47-32
NA
1.7
Nickel
7440-024-0
NA
0.20
1(049
Table B
Chromiun (Total)
7440-47-32
NA
1.7
Nickel
744O-O2—3~0
NA
0.20
128—83 1
362
1(050
Table
B
Chromiun (Total)
Nickel
1(051
Table
B
Chromiun (Total)
Nickel
1(052
TabLe
B
Chroiniun (Total)
Nickel
1(061
(Low
Zinc
St.tcategory--Less than 15
Total
Zinc)
Table
B
Caóniun
0.14
Chroiniun (Total)
5.2
Lead
0.24
Nickel
0.32
1(061
(High
Zinc
Subcategpry--greater
Table
B
Cadniun
_________
0.14
Chromiun (TotaL)
_________
5.2
Lead
__
0~4
Nickel
_________
0.32
1(062
Table 8
Chromiun (Total)
0.094
0.37
1(069 (Calciun
Sulfate Subcategory)
Tables
B
&
Cadniun
0
Lead
NA
0.025
NA
0.088
NA
NA
0.094
NA
0.37
NA
0.51
NA
0066
NA
5.2
NA
0.51
HA
5.6#~
NA
56~
7440-47-32
7440-024
NA
NA
1.7
020
7440-47-32
7440-024Q
NA
NA
1.7
0.10
7440-47-32
7440-024Q
NA
NA
1.7
0.20
7440-43-9
NA
7440-47-32
NA
7439-92-1
NA
7440-024Q
NA
than 15
Total Zinc)--effective untiL August 7.
1991
7440-43-9
7440-47-32
7439-92-1
7440-02-0
7440-47-32
NA
7439-92-1
NA
Lead
7440-43-9
NA
0.14
7439-92-1
NA
0.24
1(071
Table
B
Mercury
7439-97-6
1(083
Table
B
Nickel
7440-024.Q
1(084
Table
B
Arsenic
7440-38-2
1(086
Table
B
Chromiun (Total)
7440-47-32
Lead
7439-92-1
1(087
Table
B
Lead
7439-92-1
1(100
Table
B
Cathiun
7440-43-9
Chrorniun (Total)
7440-47-32
Lead
7439-92-1
1(101
TabLe
B
Arsenic
7440-38-2
1(102
Table
B
Arsenic
7440-38-2
1(106 (Low Mercury Si.k,category--less than 260 mg/kg Mercury--residues from RMERC)
Tables
B & Mercury
7439-97-6
NA
4,300.020
0
1(106
(Low
Mercury
SiA,category--less
than
260 mg/kg Mercury--that are
not
residues from RMERC)
TabLes
8 & Mercury
7439-97-6
NA
A0.300~~
0
1(115
Table
B
NickeL
7640-02.4-0
NA
0.32
#-
-Thoco
trootmont
ctand3rdc
hovo
L
TCLP analycie.
128—832
363
P
and
U
Listed
Wastes
CAS
No
for
Concentration
Conmercial
Regulated
Hazardous
Regulated
Concentration
(mg/L)
Nonwaste-
Waste
See
ALso
Chemical
Neme
Constituent
Hazardous
(mg/L)
Waste-
waters
Code
Constituent
waters
POlO
Table
B
Arsenic
acid
Arsenic
7440~38-2
NA
5.6
A
POll
Table
B
Arsenic
pent-
Arsenic
7440-38-2
NA
5.6 A
oxide
P012
Table
B
Arsenic
trioxide
Arsenic
7440-38-2
NA
5.6
A
P013
Table
B
Bariun
cyanide
Bariun
7440-39-3
NA
52.
P036
Table
B
Dichlorophenyl-
Arsenic
7440-38-2
NA
5.6 A
arsine
P038
TabLe
B
Diethylarsine
Arsenic
7440-38-2
NA~
56
A
P065 (Low Mercury SA~category--lessthan 260 mg/kg Mercury--residues from RMERC)
Tables
B & Mercury
Mercury
7439-97-6
NA
0.20
O
fuLminate
P065
(Low Mercury SLlcategory-
-
less than
260
mg/kg
Mercury-
-
incinerator
residues
(and
are
not
residues
from
RMERC))
Tables B &
Mercury
Mercury
7439-97-6
NA
0.025
O
fulminate
P073
Table
B
Nickel carbonyl
Nickel
7440-024.Q
NA
0.32
P074
Table
8
Nickel cyanide
Nickel
7440024Q
NA
0.32
P092 (Low Mercury SiAxategory
- -
less
than
260
mg/kg
Mercury
residues from RMERC)
Tables B &
Phenyl mercury
Mercury
7439-97-6
NA
0.20
O
acetate
P092
(Low
Mercury
S~category-
-
less
than
260
mg/kg Mercury-
-
incinerator
residues
(and are
not
residues
from
RMERC))
Tables
B &
Phenyl
mercury
Mercury
7439-97-6
NA
0.025
D
acetate
P099
Table
8
Potassiun silver
Silver
7440-22-4
NA
0.072
cyanide
P103
Table
B
Selenourea
Seleniun
7782-49-2
NA
57
P104
Table B
Silver cyanide
Silver
7440-22-4
NA
0.072
P110
Table B
Tetreethyl
Lead
Lead
7439-92-1
NA
051
P114
TabLe B
Thalliun
Seteniun
7782-49-2
NA
.7
seleni te
U032
Table B
Catciun chromate
Chromiun
(Total)
7440-47-32
NA
0.094
U051
Table B
Creosote
Lead
7439-92-1
NA
0.51
U136
Table B
Cacodylic acid
Arsenic
7440-38-2
NA
5.6
Ui44
Table B
Lead acetate
Lead
7439-92-1
NA
0.31
128—833
364
U145
Table
B
Lead phosphate
Lead
7439-92-1
HA
0.51
U146
Table
B
Lead subacetate
Lead
7439-92-1
NA
0.51
U151
(Low Mercury Subcategory-
-
less
than 260 mg/kg Mercury--residues from RMERC)
Tables B &
Mercury
Mercury
7439-97-6
NA
0.10
0
Ui51
(Low Mercury Subcategory--less than 260
tag/kg
Mercury--that
are
not
residues from RMERC)
TabLes
B
&
Mercury
Mercury
7439-97-6
HA
0.025
0
U204
TabLe
8
SeLeniun
dioxide
Seleniun
7782-49-2
NA
5.7
U205
Table
B
Seleniun sulfide
Seleniun
7782-49-2
WA
57
#A--
These
treatment
standards
have
been
based
on
EP
Leachate
analysis
but
this
does
not
preclude
the
use
of
TCLP
analysis.
*8-
-
These waste codes are
not
subcategorized
into wastewaters
and
nonwastewaters.
NA--
Not Applicable.
(Source:
Amended at 16 Iii.
Reg.
,
effective
)
Section
728.Table
B
Constituent
Concentrations
in
Waste
(CCW)
0,
F
and
K
Listed
Wastes
Waste
See Also
Regulated Hazardous Constituent
CAS
NO.
for
Concentration
Concentration
Code
Regulated
(mg/L)
Waste-
(mg/I) Nonwaste-
Hazardous
waters
waters
Constituent
0003 (Reactive cyonides subcategory--based on Cyanidoc (AmenabLe) 35 ILL. Acàn.
Code 721.123(a)(5))
Cyanides (Total)
57-12-5
ReS.
# 590
C
Cyanides
(Amenable)
57~j2-5
QJ~
D004
Table A
Arsenic
7440-38-2
5.0
HA
0005
Table
A
Bariun
7440~39~3
100.
NA
0006
TabLe
A
Caóniun
7440-43-9
1.0
HA
D007
Table A
Chramiun
(Total)
7440-47-32
5.0
NA
0008
TabLe A
Lead
7439-92-i
5.0
MA
0009
Table A
Mercury
7439-97-6
0.20
NA
0010
TabLe
A
Seleniun
7782-49-2
1.0
NA
0011
Table A
Silver
7440-22-4
5.0
NA
0012
Table
0
Endrin
720-20-8
NA
0.13 ~
D013
TabLe 0
Lindane
58-89-9
NA
0.066
A
0014
Table 0
Methoxychlor
72-43-5
NA
0.18 A
0015
Table 0
Toxaphene
8001-35-i
NA
1.3 ~
128—834
0017
TabLe 0
2,4,5-TP jSiLvexl
F0O1-F005
spent
solvents
Tables
A
&
i,1,2-Trichloroethane
Benzene
93-76-5
71-55-6
71-43-2
NA
7~9~
0.030
a
7.6
A
0.070
a
3.7
A
FOOi-F005
spent
solvents
(Pharmaceutical
Methylene
chloride
FOlD
!i~
FOil
Table A
Cyanides
Cyanides
Chromiun
Lead
Nickel
F012
Table A
Cyanides
Cyanides
Chromius
Lead
Nickel
(Total)
(Amenable)
(Total)
(Total)
(Amenable)
(Total)
industry
wastewater
subcategory)
1.9
0.1
L5
NA
0016
Table
0
2,4-0
94-75-7
365
0
HA
10.0
~
0.44
NA
F006
TabLe A
Cyanides (Total)
Cyanides
(Amenable)
Cacisiun
Chronti us
Lead
Nickel
F007
Table A
Cyanides (Total)
Cyanides (Amenable)
Chromiun (Total)
Lead
Nickel
F008
Table A
Cyanides (Total)
Cyanides
(Amenable)
Chromius
Lead
Nickel
F009
Table
A
Cyanides (Total)
Cyanides
(Amenable)
Chromiun
Lead
Nickel
Cyanides (Total)
Cyanides (Amenable)
11
0.86
1.6
0.32
0.040
0.44
19
0.1
032
0.04
0.44
1.9
0.
1~
0.32
0.04
0.44
1.
95~
0.1
0.32
004
0.44
590.
30
NA
NA
NA
NA
590
30
NA
NA
NA
590.
30.
HA
NA
HA
590.
30.
NA
NA
NA
75-09-2
57- i2-5
57- 12-5
7440-43-9
7440-47- 32
7439-92-1
7440-
024
57-12-5
57- 12-5
7440-47-32
7439-92-1
7440-024~
57-12-5
57-12-5
7440-47-32
7439-92-1
7440-024~
57-12-5
57- 12-5
7440-47-32
7439-92-1
7440-02—3Q
57-12-5
57-12-5
57- 12-5
57-12-5
7440-47-32
7439-92-1
7440-024Q
57- 12-5
57-12-5
7440
-47-32
7439-92-i
7440-
024~
57-12-5
57-i2-5
7440-47-32
110.
9.1
NA
NA
NA
110.
9.1
NA
NA
NA
1.9
0.1
0.32
0.04
0.44
1.9
0.1
0.32
0.04
0.44
1.2
0.86
0.32
(Total)
(Amenable)
(Total)
F019
Table A
Cyanides
590.
C
Cyanides
R
30.
~
Chromiun
NA
F024
(Note: F024 organic standards trust
be
treated via incineration
(INCIN))
Tables A &
2-Chloro-1,3-butadiene
126-99-8
a 0.28 A
a
0.28
~,
0
3-Chloropropene
1,1-DichLoroethane
i,2-Dichloroethane
1,2-Dichloropropane
cis-1,3-Dichloropropene
trans-i,3-Dichloropropene
107-05-1
75-34-3
107-06-2
78-87-5
10061-01-5
10061-02-6
a
0.28 ~
a
0.014 A
a
0.014 A
a
0.014 ~
a
0014
~
a
0.014
~,
a
a
a
a
a
a
0.18 ~
0.014 A
0.014 ~
0.014 ~
0.014
~
0.014 ~
128—835
366
aids
and
desiceants
ChLoroform
Nethylene chloride
Carbon tetrachloride
1,1 ,2-Trichloroethane
Trichloroethylene
Vinyl
chloride
Hexach I
orobenzene
Hexach I orobutadi ene
Hexachloroethane
Acetone
AcenaphthaLene
Acenaphthene
Acetonitrile
Acetophenone
2-AcetyLaminof
Luorene
Acrolein
Acrylonitri le
A ldrin
4-AminobiphenyL
Aniline
Anthracene
Arami
ne
ArocLor 1016
Aroclor 1221
ArocLor
1232
Aroclor
1242
Aroclor
1248
Aroclor 1254
Aroclor
1260
alpha-BHC
beta-BHC
delta- BHC
garmna-BHC
Benzene
Benzo(a)anthracene
Benzo(b)f
Luoranthene
Benzo(k)fLuoranthene
Benzo(g,h,
i)peryLene
Benzo(a)pyrene
Bromodichloromethane
Bramoform (Tn bromomethane)
Bromomethane (methyl bromide)
4-Bromophenyl
phenyl ether
n-ButyL
alcohol
Butyl benzyl phthalate
2-sec-Butyl -4,6-dinitrophenol
Carbon tetrachloride
Carbon disulfide
a
028B
a
0.059
!
&
0.059
!
&
0.17!
&
0.010
!
a
0.059
!
0.29
8
a
024!
a
0.021
!
a
0.13!
a
0.81!
a
0.059
!
0.36 B
a
0.013
!
a
0.014
B
a
0.013
!
a
0.017!
a
0.013
!
a
0.014
B
a
0.014
~
a
0.00014
!
a
000014 B
a
0.023
!
a
0.0017
8
a
0.14!
a
0059
!
a
0.055
!
a
0.059
!
a
0.0055
B
a
0.0618
a
0.35!
a
063k
a
0.118
a
0.055 ~
a
5.6k
a
0.017
8
a
0.066g
a
0.057
g
a
0014
!
a
160.A
a
3.4&
a
4.0~
NA
a
9-7&
a
140.8
NA
a
84.8
a
0068
NA
a
14.
a
4.O~
NA
a
0.928
a
0.928
a
092A
a
0.928
a
0.928
a
1.8~
a
1.8~
a
0.066k
a
0.066
a
0.066
a
0.066
a
36.A
a
8.2~
a
3.4~
a
3.4~
a
1.5~
a
82~
a
15.8
a
15.A
a
15A
a
15.~
a
26~
a
7.9~
a
2.5~
a
5.6~
NA
Bis(2-ethyLhexyl)phthalate
Hexach
Ioroethane
Chromiun (Total)
Nickel
F025
(Light
ends
sthcategory)
Chloroform
1,2-0ichloroethane
1, 1-0ichloroethyLene
Methylene
chloride
Carbon
tetrachLoride
1,1
,2-Trichloroethane
Trichloroethylene
Vinyl
chloride
F025
(Spent
filters
subcategory)
a
0.036
A
a
0.036 A
0.35
0.47
a
0.0468
a
0.21!
a
0.025
!
a
0.089g
a
0.057!
a
0054
!
a
0.054
!
a
027~
a
0.046 ~
a
0.0898
a
0057!
a
0.054
!
a
0054
!
a
0.27g
a
0055
!
a
0.055
!
6
0.055
!
a
1.8~
a
1.8~
NA
NA
a
6.2~
a
62A
a
6.2~
a
31.A
a
62~
a
6.2~
a
5.6k
a
33.~
a
6.2~
a
31.A
a
6.2~
a
6.2~
a
5.6k
a
33.8
a
37.A
a
2&A
a
30A
F039
Table
A
117-81-7
67-72-1
7440-47-32
7440-02-3:2
67-~-3
107-06-2
75-35-4
75-9-2
56-
23-5
79-00-5
79-01-6
75-01-4
67-66-3
75-9-2
56- 23-5
79-00-5
79-01-6
75-01-4
118-74-1
87-68-3
67-72-1
67-64-1
208-96-8
83-32 -9
75-05-8
96-86-2
53-96-3
107-02-8
107- 13-1
309-00-2
92-67-1
62-53-3
120-12-7
140-57-8
12674-11-2
11104-28-2
11141-16-5
53469-21-9
12672-29-6
11097-69-1
11096-82-5
319-84 -6
319-85-7
319-86-8
58-89-9
71-43-2
56-55-3
205-99-2
207-08-9
191-24-2
50-32-8
75-27-4
75-25-2
74-63-9
1.01-55-3
71-36-3
85-68-7
88-85-7
56-23-5
75-15-0
128—83 6
367
Chlordane
57-74-9
a
00033
ft
a
0.13
A
p-ChtoroaniLine
106-47-8
a
046
ft
a
16. ~
Chlorobenzene
108-90-7
&
0.057!
a
5.7 A
ChLorobenzi
Late
510-15-6
a
0.10
ft
NA
2-ChLoro-1,3-butadiene
126-99-8
0.057
B
NA
Chlorodibromomethane
124-48-1
a
0.057!
a
4ój~.~
Chloroethane
75-00-3
a
0.27!
a
6.0
A
bis(2-Chloroethoxy)methane
111-91-1
a
0.036
ft
a
7.2
~
bis(2-Chloroethyl) ether
111-44-4
s
0.033
a
7.2
3-ChLoroothyL vinyl
othar
a
0.057
ft
ChLoroform
67-66-3
a
0.0468
a
5.6
A
bis62-Chloroisoprapyl) ether
39638-32-9
a
0.055
ft
a
7.2
~
p-Chloro-m-cresol
59-50-7
a
0.018
ft
a
14.
~
Chloromethane (Methyl
chloride)
74-87-3
a
0.19!
a
33.
A
2-Chloronaphthalene
91-8-7
a
0.055
ft
a
56
A
2-Chlorophenol
95-57-8
a
0.044
ft
a
5.7 ~
3-Chloropropene
107-05-1
a
0.036
ft
a
28.
~
Chrysene
218-01 -9
a
0.059
ft
a
8.2 ~
o-Cresol
95-48-7
a
0.11
ft
a
5.6 A
Cresol (m-
and
p-isomers)
a
0778
a
3.2
A
CycLohexanone
108-94-1
a
036
ft
NA
i,2-Dibromo-3-chloropropane
96-12-8
a
0.11
ft
a
15.
~
i,2-Dibromoethane (Ethylene
106-93-4
a
0028
ft
a
15.
A
dibromide)
Dibromomethane
74-95-3
a
0.11
ft
a
45. ~
2,4-DichLorophenoxyacetic acid (2,4-
94-75-7
a
0.72
ft
a
10. A
0)
o,p’-DOD
53-19-0
a
0.023
ft
a
0.087 ~
p,p’-DDD
72-54-8
&
0.023
ft
a
0087
~
o,p’-OOE
3.424-82-6
a
0.031
ft
a
0087 A
p,p’-DOE
72-55-9
a
0.031
8
a
0087
A
o,p’-ODT
789-02-6
a
00039
ft
a
0087 A
p,p’-DDT
50-29-3
a
0.0039
ft
a
0087
A
Oibenzo(a,h)anthracene
53-70-3
a
0055
ft
a
8.2
A
Dibenzo(a.e)pyrene
192-65-4
0.061
B
m-Oichlorobenzene
541-73-1
&
0.036
B
a
6.2
A
o-Dichlorobenzene
95-50-i
a
0.088
B
a
6.2
A
p-Dichlorobenzene
106-46-7
a
0090
ft
a
62
~
DichLorodifluoromethane
75-71-8
a
0.23
ft
a
7.2
A
1,1-Dichloroethane
75-34-3
a
0.059
B
a
7.2
A
1,2-DichLoroethane
107-06-2
&
0.21
ft
a
7.2
A
i,i-Dichloroethylene
75-35-4
a
0.025
ft
a
33.
A
trans-1,2-Dichlorocthcnccthylene
a
0054
ft
a
33.
~
2,4-DichLoraphenol
120-83-2
a
0.044
ft
a
14.
~
2,6-DichLorophenol
87-65-0
a
0.044
ft
a
14.
A
1,2-Oichtoropropane
78-87-5
a
0.85
ft
a
18.
A
cis-1,3-Dichloropropene
10061-01-5
a
0.036
ft
a
18.
~
trans-1,3.Dichloropropene
10061-02-6
a
0.036
ft
a
18.
A
Dieldrin
60-57-1
a
0.017
ft
a
0.13
A
Diethyl
phthalate
84-66-2
a
0.20
ft
a
28.
A
p
0imoth-jL
anti
noaz.benzene
~0
11-3
a
0.13
NA
2,4-DimethyL
phenoL
105-67-9
a
0.036
ft
a
14
~
DimethyL
phthalate
131-11-3
a
0.047
ft
a
28.
~
Di-n-butyl
phthatate
84-74-2
a
0.057
ft
a
28.
A
1,4-Diaitrabenzene
100-25-4
a
0.32
ft
a
2.3
~
4,6-Dinitro-o-cresol
534-52-1
a
0.28
ft
a
160
~
2,4-Dinitrophenol
51-28-5
a
0.12
ft
a
160. ~
2,4-DinitrotoLuene
121-14-2
a
0.32
ft
a
140.
A
2,6-Dinitrototuene
606-20-2
a
0.55
ft
a
28.
A
Di-n-octyl phthalate
117-84-0
a
0.017
ft
a
28.
~
Di-n-propylnitrosoamine
621
-64-7
a
0.40
fta
14
~
Diphenylamine
122-39-4
0.51
B
NA
1,2-DiphenyL hydrazine
122-66-7
a
0087
ft
NA
Diphenytnitrosamine
621-64-7
0.40 B
NA
128—83
7
368
1,4-Dioxane
123-91-1
a
0.12
ft
a
170. A
Disulfoton
298-04-4
a
0.017
ft
a
6.2
A
Endosulfan
I
939-98-8
&
0.023
ft
a
0.066 ~
Endosulfan II
33213-6-5
a
0.029
ft
a
0.13
A
Endosulfan suLfate
1031-07-8
a
0029
ft
a
0.13 A
Endrin
7~-2O-8
&
0.0028
B
a
0.13
A
Endrin
aLdehyde
7421-93-4
a
0.025
ft
a
0.13
A
Ethyl
acetate
141-78-6
a
0.34
ft
a
33.
A
Ethyl cyanide
107-12-0
a
0.24
ft
NA
360.
A
Ethyl
benzene
100-41-4
a
0057
B
a
6.0
A
Ethyl ether
60-29-7
a
0.12
ft
a
160.
A
bis(2-Ethylhexyl) phthalate
117-81-7
a
0.28
ft
a
28.
~
Ethyl
methacrylate
97-63-2
a
0.14
ft
a
160.
A
Ethylene oxide
75-21
-8
a
0.12
B
HA
FMçhur
52-85-7
a
00i7
ft
a
15. A
FLuoranthene
206-44-0
a
0.068
ft
a
8.1 ~
Fluorene
86-73-7
a
0.059
ft
a
4.0
A
Fluorotrichloromethane
75-69-4
a
0020
ft
a
33..
A
HeptachLor
76-44~8
a
0.0012
B
a
0.066 ~
Heptachlor
epoxide
1024-57-3
a
0.016
ft
a
0.066
A
Hexachlorobenzene
118-74-1
a
0.055
ft
a
37
A
Hexachlorobutadiene
87-68-3
a
0.055
ft
a
28.
A
HexachlorocycLopentadiene
77-67-4
a
0.057
ft
a
3.6.
A
HexachLorodibenzofurans
a
0.000063
ft a
0.001 ~
Hexachlorodibenzo-p-dioxins
a
0000063
ft
a
0.001
~
Hexachloroethane
67-72-i
a
0.055
ft
a
28.
A
Hexachloropropene
1888-71-7
a
0.035
ft
a
28.
~
Indeno(1,2,3,-c,d)pyrene
193-39-5
a
00055
ft
a
8.2
A
Iodotnethane
74-88-4
&
0.019
B
a
65.
A
Isobutanol
78-83-1
a
5.6
ft
a
170. A
Isodrin
465-73-6
a
0.021
B
a
0.066
A
Isosafrole
120-58-1
a
0.081
ft
a
26
A
Kepone
143-50-8
a
0.0011
ft
a
0.13
A
Methacrylonitrile
126-98-7
a
0.24
ft
a
84
~
Methanol
67-50-1
56B
NA
Methapyrilene
91-80-5
a
0.081
ft
a
1.5 ~
Methoxychtor
72-43-5
a
0.25
8
a
0.18 A
3-MethyLcholanthrene
56-49-5
&
0.0055
ft
a
iS.
~
4,4-Methylene-bis-(2-chtoroaniline)
101-14-4
6
0.50
ft
a
35.
ft
Methytene chloride
75-09-2
a
0.089
ft
a
33.
A
Methyl ethyl ketone
78-93-3
&
0.28
ft
a
36.
ft
Methyl isobutyl ketone
108-10-1
a
0.14
ft
a
33.
ft
Methyl methacryLate
80-62-6
&
0.14
ft
a
160.
ft
Methyl methansulfonate
66-27-3
a
0018
ft
NA
Methyl parathion
298-00-4~Q
a
0.014
ft
a
4.6
ft
Naphthalene
91-20-3
a
0059
ft
a
3.1
ft
2-HophtyLNaphthyLamine
91-59-8
a
0.52
ft
NA
p-Nitroaniline
100-01-6
a
0.028
ft
a
28
ft
Nitrobenzene
98-95-3
a
0.068
ft
a
14.
A
5-Nitro-o-toluidine
99-55-8
a
0.32
ft
a
28
A
4-Nitrophenol
100-02-7
a
0.12
ft
a
29
ft
N-Nitrosodiethylamine
55-18-5
a
0.40
ft
a
28..
A
N-Nitrosodimethylamine
62-75-9
a
0.40
ft
NA
N-Nitroso-di-n-butyLamine
924-16-3
a
0.40
ft
a
17.
ft
H-Nitrosomethylethylamine
105-95-6
a
0.40
ft
a
2.3
ft
N-Nitrosomorpholine
59-89-2
a
0.40
ft
a
2.3
ft
N-Nitrosopiperidine
100-75-4
a
0.013
ft
a
35.
ft
N-Nitrosopyrrolidine
930-55-2
a
0.013
ft
a
35
ft
Parathion
56-38-2
a
OG3Q~Qj~
a
4.6
ft
B
Pentachlorobenzene
608-93-S
a
0055
ft
a
37.
ft
Pentachlorodibenzo-furans
a
0.000035
a
0.001
ft
0063
B
Pentachlorodibenzo-p-dioxins
a
0.000063
ft
a
0.001
ft
Pentachloronitrobenzene
82-68-8
a
0.055
ft
a
4.8
ft
128—838
369
Pentachlorophenol
87-86-5
a
0.089
ft
a
7.4
ft
Phenacetin
62-44-2
a
0.081
ft
a
16.
ft
Phenanthrene
85-01-8
a
0059
ft
a
3.1 A
PhenoL
108-95-2
a
0.039
ft
a
6.2
A
Phorate
298-02-2
a
0.021
B
a
4.6
ft
Propanenitrils
tu~nyt
syanido)
107-12-0
a
0.2~
a
3~O.
PhthaLic
anhydride
65-44-9
0.069
8
~fft
Pronanide
23950-58-5
a
0.093
B
a
1.5
ft
Pyrene
129-00-0
a
0.067
ft
a
8.2
ft
Pyridine
110-86-1
a
0.014
B
a
16.
ft
SafroLe
94-59-7
.
a
0.081
ft
a
22.
ft
SiLvex
(2,4,5-TP)
93-72-1
a
0.72
ft
a
7.9
ft
2,4,5-T
93-76-s
a
0J2
ft
a
7.9
ft
1,2,4,5-Tetrachlorobenzene
95-94-3
a
0.055
ft
a
19.
ft
TetrachLorodibenzofurans
a
0.000063
B
a
0.001
ft
TetrachLorodibenzo-p-dioxins
a
0.000063
8.
0.001
ft
2,3,7,I-T.trochloredibonao-p-dioxin
a
0000063
NA
1,1,1,2-Tetrachtoroethane
630-20-6
a
0.057
ft
a
42.
ft
1,i,2,2-Tetrachtoroethane
79-34-6
a
0.057
ft
a
42.
ft
TetrachLoroethcnoethytene
127-18-4
a
0.056
8
a
5.6
ft
2,3,4,6-Tetrachtorophenol
58-90-2
a
0.030
ft
a
37.
ft
Toluene
108-88-3
a
0.080
ft
a
28.
ft
Toxaphene
8001-35-1
a
0.0095
ft
a
1.3.ft
1,2,4-TrichLorobenzene
120-82-1
a
0.055
ft
a
19
ft
1,1,1-Trichloroethane
71-55-6
a.
0.054
ft
a
56 A
1,1,2-Trichloroethane
79-00-5
a
0.054
ft
a
5.6
ft
TrichLoroethylene
79-01-6
a
0.054
ft
a
5.6
ft
2,4,5-Trichlorophenol
95-95-4
a
0.18
ft
a
37.
ft
2,4,6-TrichLorophenoL
88-06-2
a
0.035
ft
a
37
ft
1,2,3-TrichLoropropane
96-18-4
a
O~85ft
a
28.
ft
l,l,2-TrichLoro-1~2,2-trifLuoro-
76-13-1
a
0.057
ft
a
28.
ft
ethane
Tris(2.3-dibromopropyt)phosphate
126-72-7
0.11
B
~ft
Vinyl
chloride
75-01 -4
a
0.27
ft
a
33.
ft
Xylene(s)
a
0.32
ft
a
28.
ft
Cyanides (Total)
57-12-S
a
1.2
ft
a
1.8
A
Cyonidoc
(ArnonobLo)
57-12-5
c
0.&6
NA
FLuoride
16964-48-8
a
35.
B
NA
Sulfide
8496-25-8
a
14.
ft
NA
Antimony
7440-36-0
a
19
ft
NA
Arsenic
7440-38-2
a—5..0
HA
1.4
B
Bariun
7440-39-3
a
1.2
B
HA
Berylliun
7440-41-7
a
0.82
ft
NA
Cadeiun
7440-43-9
a
0.20
ft
NA
Chromiun (Total)
7440-47-32
a
0.37
ft
NA
Copper
7440-50-8
a
1.3 8
NA
Lead
7439-92-1
a
0.28
ft
NA
Mercury
7439-97-6
a
0.15
ft
NA
Nickel
7440-024-0
a
035
ft
NA
SeLeniun
7782-49-2
a
0.82
ft
NA
Silver
7440-22-4
a
0.29
ft
NA
Thattius
7440-28-0
L4B
~fft
Vanadiun
7440-62-2
a
0.042
ft
NA
7440-66-6
iA..ft
~fft
KOO1
Table A
Naphtha(ene
91-20-3
a
0.031
ft
a
1.5
ft
PentachLorophenoL
87-86-5
a 0.031
—1-.-5
ft
0.18 A
Phenanthrene
85-01-8
a
0031
A
a
1.5
ft
Pyrene
129-00-0
a
0028
ft
a
1.5
ft
ToLuene
4O~108-88-3
a
0028
ft
a
28.
ft
Xylenes
(Total)
a
0032
A
a
33.
ft
Lead
7439-92-i
a
0.037
HA
128—839
370
1(002
Table A
Chromiun (Total)
Lead
1(003
Table
A
Chromiun
(Total)
Lead
1(004
Table
A
C~romius(Total)
Lead
1(005
Table A
Chromiun (Total)
Lead
Cyanides (Total)
1(006
Table A
Chramiun (Total)
Lead
1(007
Table A
Chromius (Total)
Lead
Cyanides (Total)
1(008
Table A
Chromiun (Total)
Lead
7440-47-32
a
30.0
ft
7439-92-1
a
3.4
ft
7440-47-32
a
2Q9
ft
7439-92-i
a
3.4
ft
7440-47-32
a
3Q9
ft
7439-92-1
a
3.4
ft
7440-47-32
a
3Q.0
ft
7439-92-1
a
3.4
ft
7440-47-32
a
2Q.9
ft
7439-92-1
a
3.4
ft
120-12-7
98-87-3
205-99-2
207-08-9
85-01-8
108-88-3
7440-47-32
7440- 024.Q
1.0
a
0.28
0.08929
0.27
0.15
0.32
0.44
3.4
ft
a
6.2ft
3-4
ft
a
3.4ft
a
60ft
HA
NA
a
2&18
A
a
28ft
a
7.2ft
a
6.Oft
7440-47-32
7439-92-1
57-12-5
a
3Q.9ft
a
3.4ft
a
0.74ft
NA
NA
NA
NA
HA
NA
NA
NA
R
Q
NA
NA
NA
NA
a
NA
NA
7440-47-32
7439-92-1
57- 12-5
a
3Q.9ft
a
3.4ft
a
O,74ft
0.1
a
6.Oft
67-66-3
67-
66-3
75-05-8
107-13-1
79-06-1
71 -43-2
57- 12-5
75-05-8
107-13-1
79-06-1
71 -43-2
57- 12-S
75-05-8
107-13-1
79-06-i
71-43-2
57- 12-5
0.1
38.
0.06
19.
0.02
21.
38.
0.06
19.
0.02
21.
38
0.06
19.
0.02
21.
60
ft
1.8
ft
1.4
ft
23
ft
0.03
ft
57-
a
1.8ft
a
1.4ft
a
23ft
a
003ft
57.
a
L8ft
a
L4A
a
23.ft
a
O.03ft
57.
1(009
!~ft
Chloroform
1(010
~ft
Chloroform
KOil
NA
Acetonitrile
Acrylonitri Ic
Acrylamide
Benzene
Cyanide (Total)
1(013
NA
AcetonitriLe
Acrylonitri le
Acrylainide
Benzene
Cyanide (Total)
1(014
~fft
Acetonitrite
Acrylonitri
le
Acrylamide
Benzene
Cyanide (Total)
1(015
Table A
Anthracene
Benzal chloride
Sun
of Benzo(b)fLuoranthene and
Benzo(k)fluoranthene
Phenanthrene
Toluene
Chrcn,ius (Total)
Nickel
1(016
~jft
Hexachlorobenzene
HexachLorobutadiene
Hexachtorocyclopentadiene
Hexach
loroethane
Tetrach Ioroethene
1(017
~ft
1,2-Dichloropropane
1,2,3-TrichLoropropane
Bis(2-chloroethyl)ether
1(018
~ft
ChLoroethane
118-74-1
87-68-3
77-47-4
67-72- 1
127-18-4
78-87-5
96-18-4
111-44-4
a
2&ft
a
5.i~ft
a
56ft
a
2&ft
a
6.Oft
a
0.033
ft
a
0.007
ft
a
0007
ft
a
0.033
ft
a
0.007 ft
aa
0.85
ftft
aa
0.85
ftft
a.
0.033
ftft
75-00-3
a
0.007
ft
127—840
371
Chloromethane
74-87-3
0.007
A
~ft
1,1-DichLoroethane
75-34-3
a
0.007
ft
a
6.0
ft
1,2-DichLoroethane
107-06-2
a
0.007
ft
a
6.0
ft
HexachLorobenzene
118-74-1
0.033
A
28.A
Hexachlorobutadiene
87-68-3
a
0.08~QQLft
a
5.6
ft
Hexachloroethane
67-72-1
a 0.OOTNA
a
28.
ft
Pentachloroethane
76-01-7
a
0.007 A
a
5.6
ft
1,i,1-Trichloroethane
71-55-6
a
0.007
ft
a
6.0
ft
1(019
NA
Bis(2-chloroethyl)ether
111-44-4
a
0.007
ft
a
5.6
ft
Chlorobenzene
108-90-7
a
0.006
ft
a
6.0
ft
Chloroform
67-66-3
a
0.OO~007Aa
6.0
ft
p”.DichLorobenzene
106-46-7
a
0.008
ft
NA
1,2-DichLoroethane
107-06-2
a
0001QQ~ft
NA6~Lft
FLuorene
86-73-7
a
0.007
ft
NA
Hexachloroethane
67-72-1
a
0.033
A
a
28.
ft
Naphthalene
91-20-3
a
0.007.ft
a
5.6
ft
Phenanthrene
85-01-8
a
0.007
A
a
5.6
ft
i,2,4,5-Tetrachlorobenzene
95-94-3
a
0017
ft
NA
TetrachLoroethene
127-18-4
a
0.007
ft
a
6.0
ft
i,2,4-Trichlorobenzene
120-82-1
a
0.023
ft
a
19.
ft
1,1,1-Trichloroethane
71-55-6
a
0.007 A
a
6.0
ft
1(020
~ft
1,2-Dichloroethane
107-06-2
a
0.007
ft
a
6.0
ft
1,i,2,2-TetrachLoroethane
79-34-6
a
0.007
ft
a
5.6
ft
Tetrachloroethene
127-18-4
a
0.007 A
a
6.0
ft
1(021
TabLe
A
Chloroform
67-66-3
a
0.046
ft
a
6.2
ft
Carbon
tetrachloride
58-23-S
a
0.057
ft
a
6.2
ft
Antimony
51-23-57440-36-
6
0.0i~a
~~~3NAA
0
1(022
TabLe A
Toluene
108-88-3
6
0060
a
0.034
A
Acetophenone
96-86-2
0.010
a
19.
ft
Diphenylamine
22-39-4
a
0.52
ft
NA
Diphenytnitrosainine
86-30-6
a
0.40
ft
NA
Sun of Diphenytamine and
Diphenyl-
NA
a
13.
ft
ni trosami no
Phenol
108-95-2
0.039
a
12.
ft
Chromiun
(TotaL)
7440-47-32
0.35
NA
Nickel
7440-02—~Q
0.47
NA
1(023
~fft
Phthatic arthydride (measured as
8S-44-9
a
0.54
ft
a
28.
ft
Phthatic acid)
1(024
~fft
Phthatic anhydride (measured as
85-4.4-9
a
0.54 A
a
28.
ft
PhthaLic acid)
1(028
Table A
1,1-DichLoroethane
75-34-3
a
0.007
ft
a
6.0 A
trans-i,2-Dichloroethene
a
0.033
ft
a
6.0
ft
Hexachlorobutadiene
87-68-3
a
0.007
ft
a
5.6
ft
Hexachloroethane
67-72-1
a
0.033
ft
a
28.
ft
Pentach(oroethane
76-01-7
a
0.033
ft
a
5.6
ft
1,1,1,2-TetrachLoroethane
630-20-6
a
0.007
ft
a
5.6
ft
1,1,2,2-TetrachLoroethane
79-34-6
a
0.007
ft
a
5.6
ft
1,1,1-Trichloroethane
71-55-6
a
0.007
ft
a
6.0
ft
1,1,2-Trichloroethane
79-00-5
a
0.007
ft
a
6.0
ft
Tetrachloroethytene
127-18-4
a
0.007
ft
a
6.0
ft
Cadeiun
7440-43-9
6.4
NA
Chromius (Total)
7440-47-32
0.35
NA
Lead
7439-92-1
0.037
NA
Nickel
7440-024..Q
0.47
NA
1(029
HA
Chloroform
67-66-3
0.46
a
6.0
ft
1,2-Dichloroethane
107-06-2
0.21
a
6:0
ft
128—84
1
372
1(032
~ft
1(042
~ft
Disulfoton
Disutfoton
Toluene
2,4-Dichtorophenol
2,6-Dichlorophenot
2,4,5-Trichtorophenol
2,4,6-TrichLorophenol
Tetrachlorophenols (Total)
Pentach
t
orophenol
7440-38-2
0.79
298-04-4
298-04-4
108-88-3
a
0.049ft
a
0.013
ft
a
0.016
ft
a
0.039
ft
a
0~.018
ft
a
0.022
ft
NA A
a
038ft
a
0.34A
a
82ft
a
7.16A
a
0.68ft
a
1.9ft
1(030
!ift
1,l-DichLoroethylene
75-35-4
0.025
a
6.0
ft
1,1,1-Trichloroethane
71-55-6
0.054
a
6.0 A
Vinyl
chloride
75-01-4
0.27
a
6.0
ft
o-Dichlorobenzene
95-50-1
a
0008 A
NA
p-Dichlorobenzene
106-46-7
a
O.0Q~QQftft
NA
Hexachlorobutadiene
87-68-3
a
0.007
A
a
5.6
ft
Hexachloroethane
67-72-1
a
0.033 A
a
28.
ft
HexachLoropropene
1888-71-7
NA
a
19. A
PentachLorobenzene
608-93-5
NA
a
28
A
Pentachloroethane
76-01-7
a
0.007 A
a
56
ft
1,2,4,S-TetrachLorobenzene
95-94-3
a
0017 A
a
14. A
Tetrachloroothanocthene
127-18-4
a
0.007
ft
a
6.0
ft
1,2,4-Trichlorobenzene
120-82-1
a
0023
ft
a
19.
ft
6
0057
ft
a
00033
ft
a
0.0Q12
ft
a
0.016
ft
a
24.A
a
O.26ft
a
0.066ft
a
0066ft
K031
Table A
Arsenic
Hexach IorocycLopentadiene
Chlordane
Heptach Ior
Heptachlor epoxide
Hexach Iorocyc
I
opentad iene
Hexach Iorocyc Iopentadiene
Acenaphthene
Anthracene
Benz(a)anthracene
Benzo(a)pyrene
Chrysene
Dibenz(a,
h)anthracene
Fluoranthene
Fluorene
lndeno(1
,2,3-cd)pyrene
Cresols
(m-
and p-isomers)
Naphthalene
o-Cresol
Phenanthrene
Phenol
Pyrene
a
0.0578
a
2.4.A
a
0.057ft
a
24A
77-47.4
57-
74.9
76-44-8
1024-57-3
77.47.4
77.47-4
83-32-9
120-12-7
56-55 -3
50-32-8
218-01-9
53-70-3
206-44-0
86-73-7
193-39-S
91-20-3
95-48-7
85-01-8
108-95-2
129-00-0
1(033
!~ft
1(034
!~ft
KO3S
!~ft
1(036
~ft
1(037
~ft
1(038
!~ft
1(060
1~ft
K041
~ft
HA
HA
a
0.59ft
NA
a
0.059
ft
NA
a
0068ft
NA
NA
a
0.77ft
a
0.059
ft
a
0..llft
a
0.059
ft
0.039
a
0.067ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
a
3.4ft
NA
a
3.4ft
NA
a
3.4ft
NA
a
8.2ft
Phorate
Phorate
Toxaphene
1,2,4,5-TetrachLorobenzene
o-Dichlorobenzene
p-Dichlorobenzene
Pentach Iorobenzene
1,2,4-Trichlorobenzene
a
O..025ft
a
0.lft
a
OO2Sft
a
0.lft
a
0.OSOB
a
28.ft
0.025
ft
a
0.1
ft
0.025
ft
a
0.1
ft
a
0.0095ft
a
26ft
1(043
ftft
298-02-2
298-02-2
8001-35-1
95-94-3
95-50-1
106-46-7
108608-93-5
120-82-1
120-83-2
87-65-0
95-95-4
88-06-2
87-86-S
a
0055
ft
a
0088ft
a
0.090ft
a
0055
ft
a
0.055
ft
a
4.4ft
a
4.4ft
a
4.4ft
a
4.4ft
a
44ft
128—842
373
1(046
Table A
Lead
7439-92-1
33-32-2208-96-8
120-12-7
71-43-2
I0-32~.1117-81-7
50-32-8
75- 15-0
218-01-9
105-67-9
100-41-4
86-73-7
91-20-3
85-01-8
108-95-2
129-00-0
0037
NA
a
0.05ft
a
0.039
ft
a
0011 A
a
O.043ft
a
0.047ft
a
0.043ft
a
0.043ft
a
0.06A
a.
0_oil A
a.
005aft
a
0.033
ft
a
0.039
ft
a
0047ft
a
0.045
ft
NA
a
28.ft
a
14.ft
a
20.ft
a
l2.ft
a
7.3ft
a
15.A
a
36A
a
14.ft
NA
a
42.ft
a
34.ft
a
3.6ft
a
36.ft
79-01-6
a
0.006ft
a
0~001ft
a
0001
ft
a
0001
A
a
0.001
ft
a
0.OOlft
a
0.001
ft
a
1.7ft
a
0.001
ft
a
0.0Olft
a
0.001
ft
a
0.001
ft
a
0.001
ft
a
0.001
ft
TetrachLoroethene
HexachLorodibenzo-p-dioxins
Hexachlorodibenzo-furans
PentachLorodibenzo-p-dioxins
Pentach Iorodibenzo- furans
Tetrachlorodibenzo-p-dioxins
TetrachLorodibenzo-furans
1(048
Table
A
Benzene
Benzo(a)pyrene
Bts(2-ethylhexyl )phthalate
Chrysene
Di-n-butyl phthaLate
Ethytbenzene
Fluorene
Maphthalene
Phenanthrene
Phenol
Pyrene
Toluene
Xylene(s)
Cyanides (Total)
Chromiun (Total)
Lead
1(049
Table A
Anthracene
Benzene
Benzo(a)pyrene
Bis(2-ethyLhexyl)phthalate
Carbon dis~jlfide
Chrysene
2,4-Dimethylphenol
Ethylbenzene
Naphthatene
Phenanthrene
Phenol
Pyrene
ToLuene
Xylene(
5)
Cyanides (Total)
Chromiun (Total)
Lead
1(050
Table
A
Benzo(a)pyrene
Phenol
Cyanides (Total)
Chromiun (Total)
Lead
1(051
Table A
Acenaphthene
Anthracene
Benzene
Benzo(a)anthracene
Benzo(a)pyrene
Bis(2-ethyLhexyl)phthalate
Chrysene
Di-n-butyl phthalate
Ethylbenzene
Fluorene
Naphthalene
Phenanthrene
PhenoL
Pyrene
71-43-2
50-32-8
117-81-7
218-01-9
84-74-2
100-41-4
86-73-7
91-20-3
85-01-8
108-95-2
129-00-0
108-88-3
57-12-5
7440-47-32
7439-92-1
120-12-7
71 -43-2
50-32-8
117-81-7
75-15-0
218-01-9
105-67-9
100-41-4
91-20-3
85-01-8
108-95-2
129-00-0
108-88-3
57-12-S
7440-47-32
7439-92-1
50-32-8
108-95-2
57-12-5
7440-47-32
7439-92-1
a
0.OI1A
a
a
0.047A
a
a
0.043ft
a
a
0.043ft
a
a
0.06ft
a
a
0.OilA
a
a
0.005
ft
a
0.033ft
a
a
0.039ft
a
a
0.047ft
a
a
0.045ft
a
a
O.OliA
a
a
0.011ft
a
a
0.038029 A a
0.2
0.037
a
0.039
ft
a
0.011
ft
a
0.047
ft
a
0.043A
a
0.011
ft
a
0.043A
a
0.033 A
a
0_oil
ft
a
0.033
ft
a
0.039
ft
a
0047ft
a
OO4Sft
a
0.011 A
a
0.011
ft
a
0.028 A
0.2
0.037
ft
a
0.047
ft
a
0.047 A
a
0.028
ft
0.2
0.037
14
ft
12.
ft
7.3
ft
15.
ft
3.6
ft
14. A
HA
42.
ft
34.
ft
36
ft
36. A
14.
ft
22.
ft
1.8 A
NA
NA
a
28.ft
a
14ft
a
12.ft
a
73ft
NA
a
15.ft
NA
a
14.ft
a
42.ft
a
34.ft
a
3.6ft
a
36.ft
a
14ft
a
22.ft
a
1.8ft
NA
NA
a
12ft
a
36A
a
i.8ft
NA
NA
128—843
374
To Iuene
Xylene(s)
Cyanides (Total)
Chro,niun
(Total)
Lead
1(052
Table A
Benzene
Benzo(a)pyrene
o-Cresol
p-Cresol
2,4-DimethylphenoL
Ethylbenzene
NaphthaLene
Phenanthrene
Phenol
ToIuene
Kylene(s)
Cyanides
(Total)
Chromiun (Total)
Lead
a
0.011
ft
a
0.011
A
a
0.028
ft
0.2
0.037
a
0.011
ft
a
0047ft
a
0.011
ft
a
0.011
ft
a
O.033a
a
0.011
ft
•
0.033
ft
a
0.039
ft
a
0.047ft
a
0.011
ft
a
0.011 A
a
0.028
ft
0.2
0.037
a
14.ft
a
22.ft
a
1.8ft
NA
HA
a
14ft
a
12.ft
a
62ft
a
62ft
NA
a
14ft
a
42ft
a 34
ft
a
3.6ft
a
14ft
a
22.ft
a
L8ft
NA
NA
Benzene
Benzo(a)pyrene
Naphthalone
Phenol
Cyanides (Total)
71-43-2
50-32-8
91-20-3
108-95-2
57-12-5
a
0.l7ftft
6
0.035
ftft
a
0.028
ftg
a
0.042A8
1.9
a
0.071
ft
a
3.6ft
a
3.4ft
a
3.4ft
1.2
108-88-3
57-12-S
7440-47-32
7439-92-1
71-43-2
50-32-8
95-48-7
106-44-5
105-67-9
100-41-4
91-20-3
85-01-8
108-95
-2
108-88-3
57-12-5
7440-47-32
7439-92-i
1(060
iift
1.61
NA
0.32
0.51
0.44
NA
NA
NA
0.32
0.04
0.44
NA
NA
NA
NA
031
NA
0.030
NA
1.6
1(061
Tables
A-4
Cacàniun
Chromius (Total)
Lead
Nickel
1(062
TabLe A
Chromiun (Total)
Lead
Nickel
1(069
Tables A &
Caánius
a
Lead
K0T1
Table A
Mercury
1(073
NA
Carbon tetrachloride
Chloroform
Hexachloroethane
Tetrachtoroethene
1,1,1-Trichloroethane
1(083
Table A
Benzene
Aniline
Diphenylamine
Diphenylni trosamine
Sun of DiphenyLamine and
DiphenyLni trosainine
Nitrobenzene
Phenol
Cycl
ohexanone
Nickel
1(084
~ft
Arsenic
1(085
~ft
Benzene
ChLorobenzene
o-Dichlorobenzene
7440-43-9
7440-47-32
7439-92-1
7440-02—.2Q
7440-47-32
7439-92-1
744O-02—2.Q
7440-43-9
7439-92-1
7439-97-6
58-23-5
67-66-3
67-72-1
127-18-4
71-55-6
71-43-2
62-53-3
22-39-4
86-30-6
98-95
-3
108-95-2
108-94-1
7440-024.Q
7440-38-2
71-63-2
108-90-7
95-50-i
a
0.057
ft
a
0.046ft
6
0.055
ft
a
0.056
ft
a
0.054
ft
a
0.14ft
a
0.81
a
0.52ft
a
0.40ft
NA
a
0.068ft
0.039
0.36
0.47
0.79
a
0.14ft
a
0.057
ft
a
0.088ft
a
6.2ft
a
6~2ft
a
30.ft
a
6.2ft
•
6.2ft
•
6.6ft
a
14ft
NA
NA
a
14.,ft
a
i4.ft
a
56ft
a
30.
NA
NA
a
4.4ft
a
4.4ft
a
4.4ft
128—844
375
m-aichlorobenzene
541-73-1
a
0.036
ft
a
4.4
ft
p-Dichlorobenzene
106-46-7
a
0~090
ft
a
4.4
ft
1,2,4-TrichLorobenzene
120-82-1
a
0.055
ft
a
4.4
ft
1,2,4,5-TetrachLorobenzene
95-94-3
a
0.055
ft
a
4.4
ft
Pentachlorobenzene
608-93-5
0.055
ft
a
4.4
ft
HexachLorobenzene
118-74-1
a
0.055
ft
a
4.4
ft
Aroclor 1016
1267~-11-2
a
0.013
ft
a
0.92
ft
ArocLor 1221
11104-28-2
a
0.014
ft
a
0.92
ft
ArocLor 1232
11141-16-5
a
0.013
ft
a
0.92
ft
Aroclor 1242
53469-21-9
a
0.017
ft
a
0.02
ft
Aroclor 1248
12672-29’6
a
0.013
ft
a
0.92
ft
Aroclor 1254
11097-69-1
a
0.014
ft
a
1.8
ft
Aroclor 1260
11096-82-5
a
0.014
ft
a
1.8 A
1(086
Table A
Acetone
67-64-1
0.28
a
160.
ft
Acetophenone
96-86-2
0.010
a
9.7
ft
Bis(2-ethyLhexyl)phthalate
117-81-7
a
0.28
ft
a
28.
ft
n-Butyl alcohol
71-36-3
5.6
a
2.6
ft
Butylbenzylphthalate
85-68-7
a
0.017
ft
a
7.9
ft
Cyclohexanone
108-94-1
0.36
NA
1,2-DichLorobenzene
95-50-1
0.088
a
6.0~ft
DiethyL phthaLate
84-66-2
a
0.20
ft
a
28.
ft
Dimethyl phthalate
131-11-3
a
0.047
ft
a
28.
ft
Di-n-butyL phthalate
84-74-2
a
0.057
ft
a
28
ft
Di-n-octyl phthalate
117-84-0
a
0.017
ft
a
2&.
ft
Ethyl
acetate
141-78-6
a
0.34
ft
a
33.
ft
EthyLbenzene
100-41-4
a
0.057
ft
a
6.0
ft
Methanol
67-56-1
a
5.6
ft
NA
Methyl
isobutyl
ketone
108-10-1
0.14
a
33
ft
Methyl ethyl
ketone
78-93-3
0.28
a
36.
ft
Methylene chloride
75-09-2
6
0.089
ft
a
33.
ft
Naphthalene
91-20-3
a
0.059
ft
a
3.1
ft
Nitrobenzene
98-95-3
a
0.068
ft
a
14.
ft
Toluene
108-88-3
a
0.080
ft
a
28.
ft
1,1,1-Trichloroethane
71-55-6
a
0.054
ft
a
56
ft
Trichloroethylene
79-01-6
a
0.054
ft
a
5.6
ft
Xylene(s) (Total)
(Total)
a
0.32
ft
a
28.
ft
Cyanides (Total)
57-12-5
1.9
1.5
ft
Chromiun (Total)
7440-47-32
0.32
NA
Lead
7439-92-1
0.037
NA
1(087
TabLe A
Acenaphthalene
208-96-8
a
0.028
ft
3.4
ft
Benzene
71-43-2
a
0.014
ft
a
0.071
ft
Chrysene
218-01-9
8
0.028
ft
a
3.4
ft
Fluoranthene
206-44-0
a
0.028
ft
a
3.4
ft
Indeno(l,2,3-cd)pyrene
193-39-S
a
0.028 A
a
3.4 A
Naphthalene
91-20-3
a
0.028
ft
a
3.4
ft
Phenanthrene
85-01-8
a
0.028 A
a
3.4
ft
Toluene
108-88-3
a
0.008
ft
a
065
ft
Xytene(s)
a
0.014
ft
a
0.07
ft
Lead
7439-92-1
0.037
NA
1(093
NA
Phthalic anhydride (measured as
85-4.4-9
a
0.54
ft
a
28.
ft
Phthalic acid)
1(094
NA
Phthalic anhydride (measured as
85-44-9
a
0.54
ft
a
28.
ft
PhthaLic acid)
1(095
1,i,1,2-TetrachLoroethane
630-20-6
0.057
a
56
ft
1,1,2,2-Tetrachloroethane
79-34-6
0057
a
5.6
ft
Tetrachloroethene
127-18-4
0.056
a
6.0 A
1,1,2.Trichloroethane
79-00-5
0.056
a
6.0
ft
Trichloroethylene
79-01-6
0.054
a
5.6
ft
Hexachloroethane
67-72-i
0.055
a
28.
ft
Pentachloroethane
76-01-7
0.0S5
a
5.6
ft
128—845
376
K100
Table A
Ca~niun
Chromiun
(Total)
Lead
7440-43-9
7440-47-32
7439-92-1
o-Nitroaniline
Arsenic
Cadeiun
Lead
Mercury
1(102
Table A
o-Nitrophenol
Arsenic
Cadeius
Lead
Mercury
a
0.27ft
0.79
0.24
0.17
0.082
a
0.028
ft
0.79
0.24
0.17
0.082
a
14A
NA
NA
NA
NA
a
l3.ft
HA
NA
NA
NA
1(096
NA
1,1,1,2-Tetrachloroethane
1,1,2,2-Tetrachloroethane
Tetrachloroethene
i,1,2-TrichLoroethane
Trichtoroethene
(Trichloroethylene)
630-20-6
79-34-6
127-18-4
79-00-5
79-01-6
541-73-1
76-01-7
120-82-1
0.057
0.057
0.056
0.054
0.056
0.036
0.055
0.055
a
a
a
a
a
a
a
a
5.6
ft
5.6 A
6.0
ft
6.0
ft
5.6
ft
5.6
ft
5.6 A
19.
ft
1,3-Dichlorobenzene
PentachLoroethane
1,2,4-TrichLorobenzene
1(097
~ft
HexachLorocyclopentadiene
Chlordane
Heptachlor
Heptachtor epoxide
77-47-4
57-74-9
76-44-8
1024-57-3
a
a
a
a
0.057
ft
03033
ft
0.0012
ft
0.016
ft
a
a
a
2.4
ft
0.26 A
0366
ft
0.066
ft
1(098
NA
Toxaphene
8001-35-1
a
0.0095
ft
a
2.6
ft
1(099
~ft
2,4-DichLorophenoxyacetic acid
Hexachlorodibenzo-p-dioxins
HexachLorodibenzofurans
PentachLorodibenzo-p-dioxins
Pentachlorodibenzofurans
TetrachLorodibenzo-p-dioxins
Tetrachlorodibenzofurans
94-75-7
a
a
a
a
a
a
a
1.OA
0.001
ft
0.001
ft
0.001 A
0.001 A
0.001
ft
0.001
ft
•
a
a
a
a
a
a
1.OA
0.001
ft
0.001
A
0.001
ft
0.001
ft
0.001
ft
0.001
ft
1(101
!ift
0.32
0.51
NA
NA
HA
7440-38-2
7440-43-9
7439-92-1
7439-97-6
7440-38-2
7440-43-9
7439-92-1
7439-97-6
62-53-3
71-43-2
51-28-5
98-95 -3
108-95-2
62-53-3
71-43-2
51-28-5
98-95-3
108-95-2
57-12-5
71-43-2
108-90-7
95-50-1
106-46-7
95-95-4
88-06-2
95-57-8
108-95-2
7439-97-6
1(103
NA
Aniline
Benzene
2,4-Dinitrophenol
Nitrobenzene
Phenot
1(104
~ft
Aniline
Benzene
2, 4-ainitrophenoL
Nitrobenzene
Phenol
Cyanides
(Total)
KIOS
Benzene
Chlorobenzene
o-DichLorobenzene
p-Dichlorobenzene
2,4,5-Trichlorophenol
2,4,6-Trichlorophenot
2-Chlorophenol
Phenol
1(106
Tables
A
&
Mercury
a
a
4$
a
0.1S
a
0.61
a
0.073
a
1.4
•
4.5
a
0.15
a
0.61
a
0.073
•
1.4
2.7
0.14
0.057
0.088
0.090
0.18
0.035
0.044
0.039
0.030
5.6
ft
a
6.Oft
a
56A
a
S.6ft
a
5.6ft
•
S.6ft
a
6.Oft
a
5.6ft
a
5.6ft
a
5.6ft
a
1.8ft
a
4.4ft
a
4.4ft
a
4.4ft
a
4.4ft
a
4.4ft
a
44ft
a
4.4ft
a
4.4ft
NA
128—84 6
377
K11S
Table A
Nickel
7440-02—3-0
0.47
NA
a
Treatment
otandordo
far
thia ar9onie ponotituont
were
eatabliohed booed ~pen
inoinoration
in
unite
operated in occerdanca with the tochnisal ro~.iiroontcof 15 Ill. Ada. Code 72~.Bubpart~Oor
725~t~part0, er baaed t~anaaebuotian. in fuel au.àetitutian unite
eperatin9
in aa.ardan..
uith
pplisebla teshnipal
r.~pIir.mento.A feolLity may
aurtify
aon~lianieuith thooc treatment otandard6
ueerdin3 te prsvioi.no in £sstien 728.197.
1ace~on onalyeia
ef
eotnpooit. eaopLao.
A. anaLyzed uaing LU E~Ilethed 9010: e~leala., 0.5-10: diatitlatien tim.u ama haur t. en. hour
and fifteen
minutes.
HA
Not
Applic3bl..
TABLE
B (CCW):
P AND U LISTED WASTES
CAS No. for
Concentration
Coannercial
Regulated Hazardous Regulated
Concentration
(mg/L) Nonwaste-
Waste
Chemical
Name
See Also
Constituent
Hazardous
(mg/I) Waste-
waters
Code
Constituent
waters
P004
Aldrin
NA
Aldrin
309-00-2
0.21
ft
0366
ft
POlO
Arsenic acid
Table A
Arsenic
7440-38-2
079
NA
P011
Arsenic
Table A
Arsenic
7440-38-2
0.79
NA
pentoxide
P012
Arsenic
trioxide
Table
A
Arsenic
7440-38-2
0.79
NA
P013
Bariun cyanide
Table A
Cyanides (Total)
57-12-S
1.9
110.
Cyanides (AmenabLe) 57-12-5
0.1
9.1
P020
2-sec-Butyl-4,6-
HA
2-sec-Butyl-4,6-di-
88-85-7
0.066
1
2.5
ft
dinitrophenot
nitrophenol
(Dinoseb)
(Dinoseb)
P021
CaLcius cyanide
~ft
Cyanides (Total)
57-12-5
1.9
110.
Cyanides (AmenabLe)
57-12-5
0.1
9.1
P022
Carbon
disulfide
Table
D
Carbon disulfide
75-15-0
0.014
NA
P024
p-ChloroaniLine
~ft
p-ChloroaniLine
106-47-8
0.46
1
16.
ft
P029
Copper cyanide
!~ft
Cyanides (Total)
57-12-5
1.9
110.
Cyanides (Amenable) 57-12-5
0.1
9.1
P030
Cyanides
Cyanides (Total)
57-12-5
1.9
110.
(solthLe salts
and coaplexes)
Cyanides (Amenable) 57-12-5
0.1
9.1
P036
DichLorophenyl-
Table A
Arsenic
7440-38-2
0.79
NA
arsino
P037
Dieldrin
NA
Dieldrin
60-57-1
1
0.017
ft
1
0.13 A
P038
DiethyLarsine
Table A
Arsenic
7440-38-2
0.79
NA
P039
aisuLfoton
NA
Disulfoton
298-04-4
0.017
1
0.1
ft
P047
4,6-Dinitro-o-
~ft
4,6-Dinitro-o-
534-52-4
1
0.28
ft
1
160.
ft
cresol
cresol
128—847
378
P048
2,4-Dinitro-
~ft
2,4-DinitrophenoL
51-28-5
1
0.12
ft
1
160.
A
phenol
P050
Endosulfan
Endosulfan
1
939-98-8
1
0.023
ft
1
0.066
ft
EndosuLfan
II
33213-6-5
1
0.029
ft
1
0.13
ft
Endosulf
an sulfate
1031-07-8
1
0.029
ft
1
0.13
ft
P051
Endrin
HA
Endrin
72-20-8
*
0.0028
ft
1
0.13 A
Endrin aldehyde
7421-93-4
1
0.025
ft
1
0.13
ft
P056
Fluoride
Table 0
Fluoride
16694-48-8
35.
NA
P059
Heptachlor
~ft
Heptachlor
76-44-8
1
0.0012 B
1
0.066
ft
Heptachior epoxide
1024-57-3
~
0016
ft
1
0.066
ft
P060
Isodrin
~ft
Isodrin
465-73-6
*
0.021
ft
1
0366
ft
P063
Hydrogen cyanide
~ft
Cyanides
(Total)
57-12-5
1.9
110.
Cyanides
(Amenable) 57-12-5
0.10
9.1
P065
Mercury
Tables
A
&
Mercury
7439-97-6
0.030
NA
fulminate
I)
P071
Methyl
parathion
~ft
Methyl
parathion
298-00-0
0.025
1
0.1
ft
P073
Nickel
carbonyl
Table A
Nickel
7440-02-3-0
0.44~
NA
P074
Nickel
cyanide
Table
A
Cyanides
(a~4-e
57-12-5
1.9
110.
Total)
Cyanides (Amenable) 57-12-5
0.10
9.1
Nickel
7440-02—2-0
0.44
NA
P077
p-Nitroaniline
~jft
p-NitroaniLine
100-01-6
1
0.028
ft
1
28.
ft
P082
N-Nitrosodi-
Table
0
N-Hitrosodimethyl-
62-75-9
1
0.40
S
NA
methylainine
amine
P089
Parathion
NA
Parathion
S6-38-2
0.025
1
0.1
ft
P092
PhenyLmercury
Tables
A
&
Mercury
7439-97-6
0.030
HA
acetate
0
P094
Phorate
NA
Phorate
298-02-2
0.025
1
0.1
ft
P097
Fanphur
NA
Fanphur
52-85-7
0325
1
0.1
ft
P098
Potassius
Cyanides (Total)
57-12-5
i9
110.
cyanide
Cyanides (AmenabLe) 57-12-S
0.10
9.1
P099
Potassius silver
Table A
Cyanides (Total)
57-12-5
1.9
110.
cyanide
Cyanides (Amenable) 57-12-5
0.1
9.1
Silver
7440-22-4
0.29
NA
P101
EthyL
cyanide
~fft
Ethyl cyanide
107-12-0
1
0.24
ft
1
360.
ft
(Propanenitrile)
(Propanenitrile)
P103
Selenourea
Table A
Selenius
7782-49-2
1
1.0
ft
NA
P104
Silver
cyanide
Table
A
Cyanides
(Total)
57-12-5
1.9
110.
Cyanides (AmenabLe)
57-12-5
0.10
9.1
Silver
7440-22-4
0.29
NA
128—848
379
P106
Sodiun cyanide
NA
Cyanides (Total)
57-12-S
1.9
110.
Cyanides (AmenabLe) 57-12-5
0.10
9.1
P110
Tetraethyl
lead
Tables A &
Lead
7439-92-1
0.040
NA
D
P113
Thallic oxide
Table D
ThalLiun
7440-28-0
*
0.14
ft
NA
P114
ThalLium
Table A
SeLenium
7782-49-2
1.0
NA
selenite
P115
ThaLlium
(1)
TabLe 0
Thallium
7440-28-0
1
0.14
ft
NA
suLfate
P119
Mznonia vanadate Table 0
Vanadium
7440-62-2
1
28. B
NA
P120
Vanadium
pent-
Table D
Vanadium
7440-62-2
1
28.
B
NA
oxide
P121
Zinc cyanide
~ft
Cyanides (Total)
57-12-5
1.9
110.
Cyanides (Amenable) 57-12-5
0.10
9.1
P123
Toxaphene
~jft
Toxaphene
8001-35-1
1
0.0095
ft
*
1.3
ft
U002
Acetone
Acetone
67-64-1
0.28
*
1.60.
ft
U003
Acetonitrile
Table D
AcetonitriLe
75-05-8
0.17
NA
0.17
U004
Acetophenone
~ft
Acetophenone
98-86-2
1
0.010
ft
i
9.7
ft
U005
2-AcetyLamino-
NA
2-AcetyLamino-
53-96-3
*
0.059
ft
I
140.
ft
fluorene
fluorene
U009
Acrylonitrile
~ft
Acrytonitrile
107-13-1
1
0.24
ft
*
84.
ft
U012
AniLine
AniLine
62-53-3
0.81
1
14.
ft
U018
Benz(a)-
~ft
Benz(a)anthracene
56-55-3
1
0.059
ft
1
8.2 A
anthracene
U019
Benzene
NA
Benzene
71-43-2
1
0.14
ft
*
36.
ft
UO22
Benzo(a)pyrene
~ft
Benzo(a)pyrene
50-32-8
1
0.061
ft
1
8.2 A
U024
Bis(2-chloro-
~ft
Bis(2-chloro-
111-91-1
0.036
1
7.2
ft
ethoxy)methane
ethoxy)methane
U025
Bis(2-chloro-
NA
Bis(2-chloro-
111-44-4
0.033
1
7.2
ft
ethyl) ether
ethyl) ether
U027
Bis(2-chloro-
~ft
Bis(2-chloro-
39638-32-9
1
0.055
ft
1
7.2 A
isopropyl) ether
isopropyL) ether
U028
Bis(2-ethyl-
!~ft
Bis(2-ethylhexyl)
117-81-7
*
0.54
ft
*
28.
ft
hexyl) pthalate
pthalate
U029
Bromomethane
NA
Bromomethane
74-83-9
1
0.11
ft
1
~
ft
(Methyl bromide)
(Methyl bromide)
UO3O
4-Bromophenyl
~ft
4-BromophenyL
101-55-3
*
0.055
ft
*
15.
ft
phenyL ether
phenyL
ether
U031
n-Butyl alcohol
~jft
n-Butyt alcohol
71-36-3
5.6
1
2.6 ft
U032
Calcium chromate
Table A
Chromium (Total)
7440-47-32
0.32
NA
128—849
380
0036
Chlordane (alpha
NA
Chtordane (alpha
57-74-9
I
0.00033 B
t
0l3 A
and gamma)
and gamma)
0037
Chtorobenzene
NA
Chlorobenzene
108-90-7
*
0057
ft
*
57
ft
0038
Chlorooenzilate
Table 0
ChLorobenzi Late
510-15-6
*
0.10 B
NA
0039
p-ChLoro-m-
p-Chloro-m-cresoL
59-50-7
*
0.018
ft
1
14.
ft
cresoL
0042
2-Chloroethyl
Table
0
2-Chloroethyt vinyl
110-75-8
0.057
NA
vinyl
0043
Vinyl
chloride
~ft
Vinyl
chloride
75-01-4
1
0.27
ft
1
33.
ft
0044
Chloroform
NA
Chloroform
67-66-3
*
0.046
ft
t
5.6
ft
U045
•Chloromethane
NA
Chloromethane
74-87-3
1
0.19
ft
~
33~ft
(Methyl
(Methyl
chloride)
chloride)
0047
2-Chloronaphtha-
NA
2-Chloronaphthalene
91-S8-7
1
0.055
ft
I
5.6
ft
Iene
U048
2-Chlorophenol
~jft
2-Chtorophenot
95-57-8
1
0.044
ft
*
5.7
ft
U050
Chrysene
~ft
Chrysene
218-01-9
I
0.059
ft
I
82
ft
U051
Creosote
Table A
Napbthalene
91-20-3
*
0.031
*
1.5
ft
Pentachlorophenol
87-86-5
*
0.18
~
7.4
ft
Phenanthrene
85-01-8
*
0331
*
1.5 A
Pyrene
129-00-0
*
0.028
1
3&.-1.5
ft
Toluene
108-88-3
1
0.028
*
~28. A
XyLenes (Total)
1
0.032
NA
33.
ft
Lead
7439-92-1
*
0.037
NA
0052
Cresols
NA
o-Cresol
95-48-7
1
0.11
ft
*
56
ft
(Cresytic acid)
CresoLs
Cm-
and p-
*
0.77
ft
t
3.2
ft
isomers)
U057
Cyclohexanone
Table 0
Cyclohexanone
108-94-1
0.36
NA
0060
DaD
o,p’-ODD
53-19-0
0.023
B
I
0.087
ft
p,p’-DDD
72-54-8
0.023
ft
*
0.087 A
U061
DOT
~ft
o,p’-DDT
789-02-6
*
0.0039
ft
1
0.087
ft
p,p’-DDT
50-29-3
*
0.0039
ft
*
0.087
ft
o,p’-DDD
53-19-0
0.023
ft
*
0.087
ft
p,p’-DDD
72-54-8
0.023
ft
*
0.087 ft
o,p’-aaE
3424-82-6
*
0.M31
ft
*
0.087
ft
p,p’-DDE
72-55-9
*
0.031
ft
*
0.087 ft
0063
Dibenzo(a,
HA
Dibenzo(a,h)-
53-70-3
*
0055
ft
*
8.2
ft
h)anthracene
anthracene
0066
1,2-Dibromo-3-
NA
1,2-Dibromo-3-
96-12-8
*
0~li
ft
*
15.
ft
ch
loropropane
chloropropane
0067
1,2-Dibromo-
NA
1,2-Dibromoethane
106-93-4
*
0.028
ft
*
15.
ft
ethane (Ethylene
(Ethylene di-
dibromide)
bromide)
0068
Dibromoethane
~fft
Dibromoethane
74-95-3
1
0.11
ft
15.
ft
128—850
381
1)069
Di-n-~ityl
NA
Di-n-butyt
84-74-2
*
0.54 A
*
28.
ft
phthalate
phthalate
UO7O
o-Dichloro-
NA
o-DichLorobenzene
95-50-1
*
0.088
ft
*
6.2
ft
benzene
1)071
m-DichLoro-
NA
m-DichLorobenzene
541-73-1
0.036
6~2
ft
benzene
0072
p-Dichloro-
p-Dichlorobenzene
104-46-7
*
0.090
ft
*
6.2
ft
benzene
0075
Dichtoro-
NA
DichLorodifLuoro-
75-71-8
*
023
B
1
7.2
ft
difLuoromethane
methane
U076
1,1-Dichloro-
~ft
1,1-DichLoroethane
75-34-3
*
0.059
ft
7.2
ft
ethane
0077
1,2-DichLoro-
NA
1,2-Dichloroethane
107-06-2
*
021
ft
I
7.2
ft
ethane
U078
1,1-DichLoro-
~ft
1,1-Dichloro-
75-35-4
*
0.025
ft
*
33.
ft
ethylene
ethylene
0079
1,2-Dichloro-
~ft
trans-1,2-Dichloro-
156-60-S
*
0.054
ft
33.
Xft
ethylene
ethylene
0080
MethyLene
NA
Nethylene chloride
7S-08-2
0.089 ~ft
33.
Xft
chLoride
0081
2,4-Dichloro-
~jft
2,4-aichlorophenol
120-83-2
0.044
~ft
14.
Aft
phenol
UO82
2,6-Dichtoro-
~ft
2,6-Dichtorophenol
87-65-0
0.044
~ft
14.
Xft,
phenol
1)083
1,2-Dichloro-
~ft
1,2-Dichloropropane 78-87-S
0.85 A8
18.
Aft
propane
11084
1,3-Dichloro-
ftft
cis-1,3-Oichloro-
10061-01-
0.036 AS
18 A
propene
propylene
trans-1,3-Dichloro-
10061-02-
0.036 AS
18.
Aft
propylene
1)088
Diethyl
NA
Diethyl phthalate
84-8~66-~
0.54 AS
28. XA
phthalate
0093
p-Dimethylamino-
Table
D
p-DimethyLaminoazo- 60-11-7
0.13 Aft
NA
azobenzene
benzene
1)101
2,4-DimethyL-
NA
2,4-Dimethylphenol
105-67-9
0.036 f-B
14.
f-A
phenoL
0102
DimethyL
NA
Dimethyl phthalate
131-11-3
0.54 NA
28.
f-ft
phthalate
U105
2,4-Dinitro-
~ft
2,4-Dinitrotoluene
121-14-2
0.32
Aft
140.
Aft
toluene
0106
2,6-Dinitro-
NA
2,6-Dinitrotoluene
606-20-2
0.55
Aft
28.
Aft
to I
uene
1)107
Di-n-octyl
NA
Di-n-octyl
117-84-0
0.54 Aft
28.
f-ft
phthaLate
phthalate
128—85 1
382
0108
1,4-Dioxane
NA
1,4-Dioxane
123-91-1
0.12 Aft
170
f-A
0111
Di-n-propyL-
~ft
Di-n-propylnitroso-
621-64-7
0.40 Aft
14. NA
ni trosoamine
amine
0112
EthyL acetate
~ft
Ethyl acetete
141-78-6
0.34
AS
33.
f-A
0117
Ethyl ether
Ethyl ether
60-29-7
0.12 Aft
160.
f-ft
0118
Ethyl meth-
NA
Ethyl methacryLate
97-63-2
0.14 Aft
160.
f-ft
acryLate
0120
FLuoranthene
NA
Ftuoranthene
206-44-0
0.068
f-B
8.2
f-A
0121
Trichloro-
NA
TrichLoro-
75-69-6
0.020
f-B
33.
f-A
monof
Luoro-
monof
luoromethane
methane
0127
Hexachloro-
HexachLorobenzene
118-74-1
0.055
f-B
37.
f-A
benzene
0128
Hexachlorobuta-
~ft
Hexachlorobutadiene 87-68-3
0.055
AS
28.
f-A
diene
0129
Lindane
alpha-BHC
319-84~6
0.0001., AS
O3~
f-A
beta-BHC
319-8S-7
0.00014 B
03M66
f-A
Delta-BHC
319-86-8
0.023
ft
0.06666 f-ft
gamna-BHC
(Lindane)
58-89-9
0.0017
ft
O3M~ Aft
0130
Hexachlorocyclo-
NA
Hexachlorocyclo-
77-47-7
0.057 A
ft
3.6 f-A
pentadiene
pentadiene
0131
Hexachloroethane
NA
Hexachloroethane
67-72-1
0.055 A
ft
28.
f-A
U134
Hydrogen
Table D
Fluoride
16964-48-8
35.
NA
fluoride
1)136
Cacodylic acid
Table
A
Arsenic
7440-38-2
0.79
NA
U137
Indeno(l,2,3-
NA
Indeno(1,2,3-c,d)-
193-39-S
0.0055
AS
8.2 f-A
c.d)pyrene
pyrene
0138
lodomethane
NA
lodomethane
74-88-4
0.19
f-S
65.
f-A
0140
Isotxityt
alcohol
~ft
IsobutyL alcohol
78-83-1
5.6
170.
f-A
0141
Isosafrole
NA
Isosafrole
120-58-1
0.081
2.6
f-A
1)142
Kepone
Kepone
143-50-8
0.0011
0.13
Aft,
0144
Lead acetate
Table
A
Lead
7439-92-1
0.040
NA
U145
Lead
phosphate
Table
A
Lead
7439-92-1
0.040
NA
0146
Lead stbacetate
Table A
Lead
7439-92-1
0.040
NA
0151
Mercury
Tables A &
Mercury
7439-97-6
0.030
NA
0
0152
Methacrylo-
NA
Methacrylonitrile
126-98-7
0.24 Aft
84.
f-ft
nitri
Ic
1)154
MethanoL
NA
Methanol
67-56-1
1)155
Methapyrilene
~ft
MethapyriLene
91-80-5
0.081
1.5
f-ft
128—852
383
0157
3-Methylchol-
NA
3-Methytchot-
56-49-S
0.0055
ft
A
15.
f-A
anthrene
anthrene
0158
4,4’-Nethylene-
~ft
MethyLenebis(2-
101-14-4
0.50 Aft
35.
f-ft
bis(2-chloro~4L.
chloro-anil.ine)
aniline)
0159
Methyl ethyl
~ft
Methyl
ethyl
ketone
78-93-3
0.28
36.
f-ft
ketone
Ul61
Methyl
isobutyL
~ft
Methyl
isobutyt
108-10-1
0.14
33.
f-ft
ketene
ketone
0162
Methyl meth-
~ft
Methyl
inethacrylate 80-62-6
0.14
160.
f-ft
acrylate
0165
Naphthalene
~ft
Haphthalene
91-20-3
0.059 Aft
3.1
f-ft
0168
2-Naphthylamine
Table
D
2-NaphthyLamine
91-59-8
0.52
f-B
NA
0169
Nitrobenzene
NA
Nitrobenzene
98-95-3
0368 AS
14.
f-A
0170
4-Nitrophenol
~ft
4-Nitrophenot
100-02-7
0.12
f-ft
29.
f-A
U172
H-Nitrosodi-n-
NA
N-Nitrosodi-n-
924-16-3
0.40
f-B
17.
f-A
butylamine
butylamine
0174
N-Nitrosodi-
NA
N-Nitrosodiethyl-
55-18-5
0.40 Aft
28.
f-ft
ethylamine
amine
0179
N-Nitroso-
~ft
N-Nitrosopiperidine 100-75-4
0.013
f-ft
3S
f-ft
piperidine
UlBO
N-Nitroso-
HA
N-Nitroso-
930-55-2
0.013 AS
35.
Aft
pyrrolidine
pyrrolidine
0181
S-Nitro-o-
~ft
5-Nitro-o-toluidine
99-55-8
0.32
f-B
28.
f-A
toLuidine
0183
Pentachloro-
NA
Pentachlorobenzene
608-93-5
0.055
f-ft
37.
f-ft
benzene
1)185
Pentachloro-
NA
Pentachioronitro-
82-68-8
0.055
f-B
4.8
f-ft
ni trobenzene
benzene
0187
Phenacetin
NA
Phenacetin
62-44-2
0.081
16.
Aft,
0188
Phenol
Phenol
108-95-2
0.039
6.2 f-A
0190
Phthalic
NA
Phthalic anhydride
85-44-9
0.54
f-ft
28.
f-ft
anhydride
(measured as Ph-
(measured as
thalic acid)
Phthalic acid)
0192
Pronainide
NA
Pronamide
23950-58-5
0.093
1.5
f-A
0196
Pyridine
~ft
Pyridine
110-86-1
0314 Aft
16~f-ft
0203
Safrole
NA
Safrole
94-59-7
0.044081
22.
f-A
0204
Selenium dioxide Table A
Selenium
7782-49-2
1.0
NA
0205
SeLenium sulfide Table A
Selenium
7782-49-2
1.0
NA
128—853
384
0207
1,2,4,5-Tetra-
NA
1,2,4,5-Tetra-
95-94-3
0355
Aft
19.
f-ft
oh
Lorobenzene
chlorobenzene
0208
1,1,1,2-Tetra-
~jft
1,1,1,2-Tetra-
630-20-6
0.057
42.
f-A
chloroethane
chloroethane
0209
1,1,2,2-Tetra-
~ft
1,1,2,2-Tetra-
79-34-S
0.057 AS
42. xA
chloroethane
chloroethane
0210
Tetrachloro-
NA
Tetrachloroethylene 127-18-4
0.056 A
5.6
f-A
ethylene
0211
Carbon tetra-
~ft
Carbon
tetra-
56-i~-5
0.057
f-B
5.6
f-A
chLoride
chloride
0214
Talliun (I)
Table D
Thallium
7440-28-0
0.14
f-B
NA
acetate
U2IS
ThaLLium (I)
Table
0
Thallium
7440-28-0
0.14
f-B
NA
carbonate
U216
Thallium (I)
Table D
Thallium
7440-28-0
0.14
f-B
HA
chloride
U217
Thallium
(I)
Table
a
Thallium
7440-28-0
0.14
f-S
NA
nitrate
U220
Totuene
NA
Toluene
108-88-3
0.080
f-B
28.
f-A
U225
Tribromomethane
~ft
Tribromomethane
75-25-2
0.63 f-B
15.
f-A
(Bromoform)
(Bromoform)
0226
l,1,1-Trichloro-
~ft
1,1,1-Trichloro-
T1~55-6
0.054
f-B
5.6
f-A
ethane
ethane
0227
1,1,2-Trichloro-
~ft
1,1,2-Trichloro-
79-00-5
0.054
f-B
ethane
ethane
0228
Trichtoro-
!~ft
TrichIoroethylene
79-01-6
0.054
f-B
5.6
f-ft
ethylene
0235
tris-C2,3-Di-
~ft
tris-(2,3-Dibromo-
126-72-7
0.025
0.10
f-ft
bromopropyl)-
propyt)-phosphate
phosphate
0239
XyLenes
NA
Xylene
~
0.32
f-ft
28.
f-A
0240
2,4-Dichloro-
NA
2,4-Dichloro-
94-75-7
0.72
10.
f-A
phenoxyacetic
phenoxyacetic acid
acid
0243
Hexachtoro-
~ft
Hexachloropropene
4.QUjftftft-71-7
0398035
28.
propene
U247
Methoxychlor
~jft
Methoxychlor
72-43-5
0.25 AS
0_la f-A
f-A
Treatment
standards
for
this
organic constituent were established based ~.ponincineration in units
operated
in
accordance
with the technical requirements of
35
III.
Ada.
Code 724.Subpart
OQ
or
725.Subpart
QQ,
or
based t.pon
contustion
in
fuel substitution units operating
in accordance
with
applicable technical requirements. A facility
may
certify compliance with these treatment standards
according to provisions
in
Section
728.107.
f-B
Based
on analysis of composite
samples
As
analyzec,
using
SW-846 Method 9010
or
9012
sampLe size: O.5-10j.Qj;
distillation time: one hour
128—854
385
to
one
hour
~~fifteen
minutes.
D
Reserved.
NA
Not
Applicable.
(Source:
Amended
at
16
Iii.
Reg.
,
effective
)
Section 728.Table C Technology Codes and Description of
Technology-Based Standards
Technology
code Description of technology—based standard
ADGAS
Venting
of
compressed
gases
into
an
absorbing
or
reacting media
(i.e.,
solid or liquid) --venting can be
accomplished through physical release utilizing
values/piping; physical penetration of the container;
and/or penetration through detonation.
AMLGN
Amalgamation
of
liquid,
elemental
mercury
contaminated
with
radioactive
materials
utilizing
inorganic
reagents
such as copper,
zinc,
nickel, gold,
and sulfur that
result
in
a
nonhiquid,
semi-solid amalgam and thereby
reducing-potential emissions of elemental mercury
vapors
to
the
air.
BIODG
Biodegradation of organics or non—metallic inorganics
(i.e.,
degradable
inorganics
that
contain
the
elements
of
phosphorus,
nitrogen,
and
sulfur)
in
units
operated
under either aerobic or anaerobic conditions such that
a surrogate compound or indicator parameter has been
substantially reduced in concentration in the residuals
(e.g., Total OrganicCarbon can often be used as an
indicator parameter for the biodegradation of many
organic constituents that cannot be directly analyzed
in
wastewater
residues).
CARBN
Carbon adsorption (granulated or powdered)
of
non—metallic inorganics, organo—metalhics,
and/or
organic constituents, operated such that a surrogate
compound or indicator parameter has not undergone
breakthrough
(e.g.,
Total
Organic
Carbon
can
often
be
used as an indicator parameter for the adsorption of
many organic constituents that cannot be directly
analyzed in wastewater residues).
Breakthrough occurs
when the carbon has become saturated with the
constituent
(or indicator parameter)
and substantial
change in adsorption rate associated with that
constituent
occurs.
CHOXD
Chemical
or
electrolytic
oxidation
utilizing
the
following oxidation reagents
(or
waste
reagents)
or
128—855
386
combinations
or
reagents:
1)
Hypochlorite
(e.g. bleach);
2)
chlorine;
3)
chlorine dioxide;
4)
ozone or UV (ultraviolet light) assisted ozone;
5)
peroxides;
6)
persulfates;
7)
perchiorates;
8)
permangantes;
and/or
9)
other
oxidizing
reagents
of
equivalent
efficiency,
performed in units operated such that a surrogate
compound or indicator parameter has been substantially
reduced
in
concentration
in
the
residuals
(e.g.,
Total
Organic
Carbon
can
often
be
used
as
an
indicator
parameter for the oxidation of many organic constit-
uents that cannot be directly analyzed in wastewater
residues).
Chemical
oxidation
specifically
includes
what
is
commonly
referred
to
as
alkaline
chlorination.
CHRED
Chemical
reduction
utilizing
the
following
reducing
reagents
(or
waste
reagents)
or
combinations
of
reagents:
1)
Sulfur dioxide;
2)
sodium,
potassium,
or
alkali
salts
of
sulfites,
bisulfites, metabisulfites,
and polyethylene glycols
(e.g., NaPEG and KPEG);
3)
sodium hydrosulfide;
4)
ferrous salts; and/or
5)
other reducing reagents of equivalent efficiency,
performed
in
units
operated
such
that
a
surrogate
compound or indicator parameter has been substantially
reduced in concentration in the residuals
(e.g.,
Total.
Organic Halogens can often be used as an indicator
parameter for the reduction of many halogenated organic
constituents that cannot be directly analyzed in
wastewater
residues).
Chemical
reduction
is commonly
used for the reduction of hexavalent chromium to the
trivalent
state.
128—856
387
DEACT
Deactivation to remove the hazardous characteristics of
a waste due to its ignitability, corrosivity, and/or
reactivity.
FSUBS
Fuel
substitution
in
units
operated
in
accordance
with
applicable technical operating requirements.
HLVIT
Vitrification of high level mixed radioactive wastes in
units in compliance with all applicable radioactive
protection requirements under control of the Nuclear
Regulatory Commission.
IMERC
Incineration of wastes containing organics and mercury
in units operated in accordance with the technical
operating
requirements
of
35
Ill.
Adin.
Code
724.Subpart
O or 725.Subpart 0.
All wastewater and nonwastewater
residues derived from this process must then comply
with the corresponding treatment standards per waste
code with consideration of any applicable subcategories
(e.g., High or Low Mercury Subcategories).
INCIN
Incineration
in
units
operated
in accordahce with the
technical
operating
requirements
of
35
Ill.
Adm.
Code
724..Subpart
0
or
725.Subpart
0.
LLEXT
Liquid-liquid
extraction
(often
referred
to
as
solvent
extraction)
of organics from liquid wastes into an
immiscible solvent for which the hazardous constituents
have
a
greater
solvent
affinity,
resulting
in
an
extract high in organics that must undergo either
incineration, reuse as a fuel,
or other recovery/reuse
and
a
raffinate
(extracted
liquid
waste)
proportionately low in organics that must undergo
further
treatment
as
specified
in
the
standard.
MACRO
Macroencapsulation
with
surface
coating
materials
such
as polymeric organics (e.g. resins and plastics) or
with
a
jacket
of
inert
inorganic
materials
to
substantially reduce surface exposure to potential
leaching media.
Macroencapsulation specifically does
not include any material that would be classified as a
tank
or container according to 35 Ill.
Ada.
Code
720.
110.
NEUTR
Neutralization
with
the
following
reagents
(or
waste
reagents) or combinations of reagents:
1)
Acids;
2)
bases;
or
128—85 7
388
3)
water
(including wastewaters) resulting in a pH greater
than
2 but less than 12.5 as measured in the aqueous
residuals.
NLDBR
No land disposal based on recycling.
PRECP
Chemical precipitation of metals and other inorganics
as insoluble precipitates of oxides, hydroxides,
carbonates,
sulfides,
sulfates, chlorides,
flouridesfluorides, or phosphates.
The following
reagents
(or waste reagents)
are typically used alone
or in combination:
1)
Lime
(i.e., containing oxides and/or hydroxides of
calcium
and/or
magnesium;
2)
caustic
(i.e.,
sodium and/or potassium hydroxides;
3)
soda ash (i.e., sodium carbonate);
4)
sodium
sulfide;
5)
ferric
sulfate
or
ferric
chloride;
6)
alum; or
7)
sodium sulfate.
Additional floculating, coagulation,
or
similar
reagents/processes
that
enhance
sludge
dewatering
characteristics
are not precluded from use.
RBERY
Thermal
recovery
of
Beryllium.
RCGAS
Recovery/reuse of compressed gases including techniques
such as reprocessing of the gases for reuse/resale;
filtering/adsorption of impurities; remixing for direct
reuse ~
resale;
and use of the gas as a fuel source.
RCORR
Recovery of acids or bases utilizing one or more of the
following
recovery
technologies:
1)
Distillation
(i.e., thermal concentration);
2)
ion exchange;
3)
resin or solid adsorption;
4)
reverse osmosis; and/or
5)
incineration for the recovery of acid-—
Note:
this does not preclude the use of other physical
phase
separation
or
concentration
techniques
such
as
128—858
389
decantation, filtration (including ultrafiltrat..~J)
and centrifugation, when used in conjunction with
t
above listed recovery technologies.
RLEAD
Thermal recovery of lead in
secondary
lead
smelterE
RNERC
Retorting or roasting in a thermal processing unit
capable of volatilizing mercury and subsequently
condensing the volatilized mercury for recovery.
‘i
retorting or roasting unit (or facility) must be
subject to one or more of the following:
a)
A National Emissions Standard for Hazardous Air
Pollutants
(NESHAP)
for mercury
(40
CFR 61,
Subpart
b)
A Best Available Control Technology
(BACT)
or a Lo~
Achievable Emission Rate
(LAER) standard for mercur
imposed pursuant to a Prevention of Significant
Deterioration
(PSD) permit
(including 35 111. A4m.
201 through 203); or
c)
A state permit that establishes emission limitation
(within meaning of Section
302 of the Clean Air Act
for mercury, including a permit issued pursuant to
Ill. Ada. Code 201.
All wastewater and nonwastewat
residues derived from this process must then coi
with the corresponding treatment standards per
Svc~t
code with consideration of any applicable subcatego
(e.g., High or Low Mercury Subcategories).
RNETL
Recovery of metals or inorganics utilizing one or
in
of the following direct physical/removal technologi
1)
Ion exchange;
2)
resin or solid (i.e.,
zeolites) adsorption;
3)
reverse osmosis;
4)
chelation/solvent extraction;
5)
freeze crystalization;
6)
ultrafiltration; and/or 4—
fl
simple precipitation
(i.e.,
crystalization)
Note: this does not preclude the use of other physical p
separation or concentration techniques such as decantati
filtration
(including ultrafiltration),
and centrifugati
when used in conjunction with the above listed recovE
technologies.
128—859
390
RORGS
Recovery of organics utilizing one or more of the
following
technologies:
1)
Distillation;
2)
thin film evaporation;
3)
steam. stripping;
4)
carbon adsorption;
5)
critical fluid extraction;
6)
liquid-liquid extraction;
7)
precipitation/crystallization (including freeze
crystallization);
or
8)
chemical phase separation techniques
(i.e.,
addition of
acids,
bases,
deiuulsifiers, or similar chemicals);
Note:
This does not preclude the use of other physical phase
separation
techniques
such
as
decantation,
filtration
(including
ultrafiltration),
and
centrifugation,
when
used
in conjunction with the above listed recovery technologies.
RTHRM
Thermal
recovery of metals or inorganics from
nonwastewaters in units defined as cement kilns, blast
furnaces,
smelting,
melting
and
refining
furnaces,
combustion
devices
used
to
recover
sulfur values from
spent sulfuric acid and “other devices” determined by
the Agency pursuant to 35 Ill.
Adin. Code 720.110,
the
definition
of
“industrial
furnaces”.
RZINC
Resmelting in hicth temperature metal recovery units for
the purpose of recovery of zinc high tcinperature metal
recovery unic3.
STABL
Stabilization with the following reagents
(or waste
reagents)
or combinations of reagents:
1)
Portland cement; or
2)
lime/pozzolans
(e.g., fly ash and cement kiln
dust)--this does not preclude the addition of reagents
(e.g.,
iron salts,
silicates,
and clays) designed to
enhance the set/cure time, and/or compressive strength,
or to overall reduce the leachability of the metal or
inorganic.
SSTRP
Steam stripping of organics from liquid wastes
128—860
391
utilizing direct application of steam to the wastes
operated such that liquid and vapor flow rates,
as well
as, temperature and pressure ranges have been
optimized, monitored, and maintained.
These operating
parameters are dependent upon the design parameters of
the unit such as, the number of separation stages and
the internal column design.
Thus, resulting in a
condensed extract high in organics that must undergo
either incineration, reuse as a fuel, or other
recovery/reuse and an extracted wastewater that must
undergo further treatment as specified in the standard.
WETOX
Wet air oxidation performed in units operated such that
a surrogate compound or indicator parameter has been
substantially reduced in concentration in the residuals
(e.g., Total Organic Carbon can often be used as an
indicator
parameter
for
the
oxidation
of
many
organic
constituents that cannot be directly analyzed in
wastewater residues).
WTRRX
Controlled reaction with water for highly reactive
inorganic or organic chemicals with precautionary
controls for protection of workers from potential
violent reactions as well as precautionary controls for
potential emissions of toxic/ignitable levels of gases
released during the reaction.
Note
1:
When a combination of these technologies
(i.e., a
treatment
train)
is
specified
as
a
single
treatment
standard, the order of application is specified in
Table D by indicating the five letter technology code
that
must
be
applied
first,
then
the
designation
“fb.”
(an abbreviation for “followed by”),
then the five
letter
technology code for the technology that must be
applied next,
and so on.
Note
2:
When
more than one technology (or treatment train)
are
specified as alternative treatment standards, the five
letter technology codes
(or the treatment trains)
are
separated by a semicolon
(;)
with the last technology
preceded by the word “OR”.
This indicates that any one
of these BDAT technologies or treatment trains can be
used for compliance with the standard.
(Source:
Amended at 16 Ill.
Reg.
,
effective
)
Section 728.Table D Technology-Based Standards by
RCRA
Waste Code
128—86 1
392
Waste See
CAS No.
Technolo- Technolo- Waste Descriptions
Codes Also
gy Code,
gy Code,
and/or Treatment
Waste—
Nonwaste— Subcategory
waters
waters
DOOl.
~
NA
DEACT
NA
Ignitable Liquids
based on 35
Ill..
Ada.
Code 721.121(a)
(1)—wastewaters
DOOl
~th
NA
NA
DEACT
Ignitable Liquids
based on 35 Ill.
Adm. Code 721.121(a)
(1)-Low
TOC
Ignitable Liquids
Subcategory--Less
than 10
total
organic carbon
DOOl
~
NA
NA
FSUBS;
Ignitable
Liquids
RORGS;
or based on 35 Ill.
INCIN
Adm. Code 721.121(a)
(1)-High TOC
Ignitable Liquids
Subcategory——Greater
than or equal to 10
total organic carbon
DOOl
~
NA
NA
DEACT~~ Ignitable compressed
gases based on 35
Ill. Adm. Code
721.121(a)
(3)
DOOl
~
NA
NA
DEACT
Ignitable reactives
based
on
35
Ill.
Ada.
Code
721.121(a)
(2)
DOOl
~
NA
DEACT
DEACT
Oxidizers based on
35 Ill. Ada. Code
721.121(a)
(4)
D002
NA
NA
DEACT
DEA~T
Acid
subcategory
based on 35
Ill.
Ada. Code 721.122(a)
(1)
128—862
393
D002
~
NA
DEACT
DEACT
Alkaline subcategory
based on 35 Ill.
Adin.
Code 721.122(a)
(1)
D002
NA
NA
DEACT
DEACT
Other corrosives
based on 35 Ill.
Ada.
Code
721.122(a)
(2)
D003
~
NA
DEACT
DEACT
Reactive sulfides
(may not
(may not
based on 35
111.
Ada.
Code
721.123
(a)
diluted)
diluted)
(5)
D003
NA
NA
DEACT
DEACT
Explosives based on
35 Ill. Adm. Code
721.123(a)(6),
(7)
and
(8)
D003
~
NA
NA
DEACT
Water reactives
based on 35 Ill.
Ada. Code 721.123(a)
(2),
(3) and
(4)
D003
NA
NA
DEACT
DEACT
Other reactives
based on 35 Ill.
Adm. Code 721.123 (a)
(1)
D006
~
7440-43-9
NA
RTHERM
Cadmium~containing
batteries
D008
~
7439-~97- NA
RLEAD
Lead acid batteries
(Note:
This
standard only
applies to lead acid
batteries that are
identified as
RCRA
hazardous wastes and
that
are
not
excluded elsewhere
from regulation
under the land
disposal re-
strictions of this
Part or exempted
under other regula-
tions
(see 35 Ill.
Adm. Code 726.180).)
128—8 63
394
D009
Tables
7439-S2.7-6 NA
IMERC; or Mercury:
(High
A
& B
RMERC
Mercury
Subcategory--grea
than or equal to
mg/kg total
Mercury——contains
mercury and organ
(and are not mci:
erator residues))
D009
Tables
7439-~7-6NA
RMERC
Mercury:
(High
A
& B
Mercury
Subcategory——grea’
than
or
equal
to
mg/kg total
Nercury——inorgani
(including
incinerator residi
and residues from
RNERC))
D012
Table B 72-20-8
BIODG; or NA
Endrin
INCIN
D013
Table
B
58-89-9
CARBN;
or
NA
Lindane
INCIN
D014
Table
B
72-43-u
WETOX;
or
NA
Methoxychlor
INCIN
D015
Table B 8001—35—1
BIODG; or NA
Toxaphene
INCIN
D016
Table
B
94-75-7
CHOXD;
NA
2,4-D
BIODG;
or
INCIN
D017
Table B 93-72-1
CHOXD; or NA
2,4,5—TP
INCIN
F005
Tables
79-46-9
(WETOX
or
INCIN
2-Nitropropane
A
& B
CHOXD)
fb
CARBN;
or
INCIN
F005
Tables
110-80-5
BIODG; or INCIN
2-Ethoxyethanol
A&B
INCIN
F024
Tables
NA
INCIN
INCIN
A&B
128—864
395
K025
~
NA
LLEXT
f.b
INCIN
Distillation bottoms
SSTRIP fb
from the production
CARBN;
or
of
nitrobenzene
by
INCIN
the nitration of
benzene
K026
~
NA
INCIN
INCIN
Stripping still
tails from the pro-
duction of methyl
ethyl pyridines
K027
Zj~
NA
CARBN;
or
FSUBS;
or Centrifuge and
INCIN
INCIN
distillation
residues from
toluene diisocyanate
production
K039
NA
NA
CARBN; or
FSUBS; or Filter cake from the
INCIN
INCIN
filtration of di-
ethylphosphoro—
dithioc acid in the
production of phor-
ate
K044
NA
NA
DEACT
DEACT
Wastewater treatment
sludges from the
manufacturing
and
processing of
explosives
K045
NA
DEACT
DEACT
Spent carbon from
the treatment of
wastewatsr con-
taining explosives
K047
Ij~,
NA
DEACT
DEACT
Pink/red water from
TNT
operations
1(061
Table B NA
NA
NLDB11
Emission control
du3t/Gludge from the
primary production
of 3tcel in electric
furnacer3 (High Zinc
Cubcategory--greater
than or equal to 15
total
Zinc)
128—8 65
396
1(069
Tables
NA
NA
RLEAD
Emission control
A
& B
dust/sludge from
secondary lead
smelting:
Non—
Calcium Sulfate Sub-
category
K106
Tables
NA
NA
R14ERC
Wastewater treatment
A
& B
sludge from the
mercury cell process
in chlorine pro-
duction:
(High
Mercury Subcategory-
greater than or
equal to 260 mg/kg
total
mercury)
K1l3
~
NA
CARBN; or FSUBS;
or
Condensed
liquid
INCIN
INCIN
light ends from the
purification of
toluenediamine
in
the
production
of
toluenediamine via
hydrogenation
of
di-
nitrotoluene
K114
~
NA
CARBN;
or
FSUBS;
or
Vicinals
from
the
INCIN
INCIN
purification
of
tol-
uenediemeamine in
the production of
toluenediamine
via
hydrogenation of
dinitrotoluene
1(115
~
NA
CARBN;
or
FSiJBS; or Heavy ends from the
INCIN
INCIN
purification of
toluenediiameamine in
the
production
of
toluenediamine via
hydrogenation of di-
nitrotoluene
1(116
~
NA
CARBN; or FSUBS; or Organic condensate
INCIN
INCIN
from the solvent
recovery column in
the production of
toluene diisocyanate
via phosgenation of
toluenediamine
128—866
397
POOl
NA
81-81-2
(WETOX or FSUBS; or Warfarin (0.3)
CHOXD)
fb INCIN
CARBN;
or
INCIN
P002
~L&
591-08-2
(WETOX or INCIN
1-Acetyl-2-thiourea
CHOXD)
fb
CARBN; or
INCIN
P003
Zi~
107-02-8
(WETOX or FSUBS; or Acrolein
CHOXD)
fb INCIN
CARBN;
or
INCI
NNA
P005
~
107-18-6
(WETOX
or
FSUBS;
or
Allyl
alcohol
CHOXD)
fb INCIN
CARBN; or
INCIN
P006
~
20859-73-8
CHOXD;
CHOXD;
Aluminum phosphide
CHRED; or CHRED;
or
INCIN
INCIN
P007
~
2763-96-4
(WETOX
or
INCIN
5-Aminoethyl
3-
CHOXD)
fb
isoxazolol
CARBN;
or
INCIN
P008
~
504-24-5
(WETOX or INCIN
4-Aiuinopyridine
CHOXD)
fb
CARBN;
or
INCIN
P009
~
131-74—8
CHOXD;
FSUBS;
Anunonium
picrate
CHRED;
CHOXD;
CARBN;
CHRED; or
BIODG; or INCIN
INCIN
P014
~
108-95-5
(WETOX or INCIN
Thiophenol
(Benzene
CHOXD)
fb
thiol)
CARBN; or
INCIN
P015
IfA
7440-41-7
NAE~1~T~
RNETL;
or Beryllium dust
or RTHRN
RTHRN
128—867
398
P016
~
542-88-1
(WETOX or INCIN
Bis(chloromethyl)-
CHOXD)
fb
ether
CARBN;
or
INCIN
P017
NA
598—31-2
(WETOX or INCIN
Bromoacetone
CHOXD)
Lb
CARBN; or
INCIN
P018
N~A
357-57-3
(WETOX or INCIN
Brucine
CHOXD)
fb
CARBN; or
INCIN
P022
Table B 75-15-0
NA
INCIN
Carbon disulfide
P023
~
107-20-0
(WETOX or INCIN
Chioroacetaldehyde
CHOXD)
Lb
CARBN; or
INCIN
P026
NA
5344-82-1
(WETOX or INCIN
1-(o-Cblorophenyl)-
CHOXD)
fb
thiourea
CARBN;
or
INCIN
P027
~
542-76-7
(WETOX or INCIN
3-Chloropropio-
CHOXD)
Lb
nitrile
CARBN; or
INCIN
P028
~
100-44-7
(WETOX or INCIN
Benzyl chloride
CHOXD)
Lb
CARBN;
or
INCIN
P031
NA
460-19-5
CHOXD;
CHOXD;
Cyanogen
WETOX; or WETOX; or
INCIN
INCIN
P033
~
506-77-4
CHOXD;
CHOXD;
Cyanogen chloride
WETOX; or WETOX; or
INCIN
INCIN
P034
NA
131-89-5
(WETOX or INCIN
2-Cyclohexyl—4,6—di-
CHOXD)
fb
nitrophenol
CARBN; or
INCIN
128—868
399
P040
~
297-97-2
CARBN; or FSUBS; or O,O-Diethyl 0-
INCIN
INCIN
pyrazinyl
phospho~
thioate
P041
~
311-45-5
CARBN;
or
FSUBS; or Diethyl-p-nitro-
INCIN
INCIN
phenyl phosphate
P042
~
51-43-4
(WETOX or INCIN
Epinephrine
CHOXD)
fb
CARBN;
or
INCfl~
P043
~
55-91-4
CARBN;
or
FSUBS;
or
Diisopropylfluoro-
INCIN
INCIN
phosphate
(DFP)
P044
NA
60-51-5
CARBN; or FSUBS;
or
Dimethoate
INCIN
INCIN
P045
NA
39196-18-4
(WETOX or INCIN
Thiofanox
CHOXD)
fb
CARBN;
or
INCIN
P046
~
122-09-8
(WETOX
or
INCIN
alpha,alpha-Di-
CHOXD)
Lb
methylphenethylami
CARBN;
or
INCIN
P047
NA
534-52-1
(WETOX
or
INCIN
4,6-Dinitro-o-cre~
CHOXD)
fb
salts
CARBN;
or
INCIN
P049
NA
541-53-7
(WETOX
or
INCIN
2,4-Dithiobiuret
CHOXD)
Lb
CARBN;
or
INCIN
P054
~
151—56-4
(WETOX or INCIN
Aziridine
CHOXD)
Lb
CARBN; or
INCIN
P056
Table B 7782—41—4
NA
ADGAS fb
Fluorine
NEUTR
P057
NA
640—19—7
(WETOX or INCIN
Fluoroacetamide
CHOXD)
Lb
CARBN;
or
INCIN
128—869
400
P058
~U1
62-74-8
(WETOX
or
INCIN
Fluoroacetic
aci
CHOXD)
fb
sodium salt
CARBN;
or
INCIN
P062
~
757-58-4
CARBN;
or
FSUBS
or
Hexaethyltetra—
INCIN
INCIN
phosphate
P064
~
624-83-9
(WETOX or INCIN
Isocyanic acid,
CHOXD)
fb
ethyl
ester
CARBN;
or
INCIN
P065
Tables
628-86-4
NA
RNERC
Mercury fulminat~
A & B
(High Mercury SuJ
category——greate:
than or equal to
mg/kg total
Mercury--either
cinerator residu
or
residues
from
RMERC)
P065
Tables
628-86-4
NA
IMERC
Mercury fulminat
A
& B
(All nonwastewat
that are not
incinerator resi’
or are not residi
from RNERC;
rega’
less of Mercury
Content)
P066
~A
16752-77-5
(WETOX or INCIN
Methomyl
CHOXD)
fb
CARBN;
or
INCIN
P067
NA
75-55-8
(WETOX
or
INCIN
2-Methylaziridin
CHOXD)
Lb
CARBN;
or
INCIN
P068
~
60-34-4
CHOXD;
FSUBS;
Methyl hydrazine
CHRED;
CHOXD;
CARBN;
CHRED;
OR
BIODG;
or INCIN
INCIN
128—870
401
P069
~
75-86—5
(WETOX
or
INCIN
Methyllactonitrile
CHOXD)
fb
CARBN;
or
INCIN
P070
NA
116-06-3
(WETOX
or
INCIN
Aldicarb
CHOXD)
Lb
CARBN;
or
INCIN
P072
~
86-88—4
(WETOX or INCIN
1-Naphthyl-2-thio-
CHOXD)
fb
urea
CA.RBN;
or
INCIN
P075
NA
54-11-5k A (WETOX or INCIN
Nicotine and salts
CHOXD)
Lb
CARBN;
or
INCIN
P076
~1A
10102—43-9
ADGAS
ADGAS
Nitric
oxide
P078
~
10102-44-0
ADGAS
ADGAS
Nitrogen
dioxide
P081
~
55-63-0
CHOXD;
FSUBS;
Nitroglycerin
CHRED;
CHOXD;
CARBN;
CHRED;
or
BIODG; or INCIN
INCIN
P082
Table B 6-&~-75-9
NA
INCIN
N-Nitrosodimethyl-
amine
P084
~
4549-40-0
(WETOX or INCIN
N-Nitrosomethyl-
CHOXD)
fb
vinylamine
CARBN;
or
INCIN
P085
~
152-16—9
CABBN;
or
FSUBS;
or
Octamethylpyro-
INCIN
INCIN
phosphoramide
P087
~
20816-12-0 NA RMETL: RMETL;
or
Osmium
tetroxide
or
RTHRN
RTHRN
P088
~
14 5-73—3
(WETOX
or
FSUBS;
or
Endothall
CHOXD)
fb INCIN
CARBN;
or
INCIN
128—87 1
402
P092
Tables
62-38-4
NA
RMERC
Phenyl mercury
A & B
acetate:
(High
Mercury Sub-
category——greater
than or equal to 260
mg/kg total
Mercury--either in-
cinerator residues
or residues from
RMERC)
P092
Tables
62-38-4
NA
IMERC; or Phenyl mercury
A
& B
RMERC
acetate:
(All
nonwastewaters that
are not incinerator
residues and are not
residues
from
RNERC:
regardless
of
Mercury
Content)
P093
NA
103-85-5
(WETOX
or
INCIN
~j~Pheny1thiourea
CHOXD)
Lb
CARBN;
or
INCIN
P095
~
75-44-5
(WETOX
or
INCIN
Phosgene
CHOXD)
fb
CARBN;
or
INCIN
P096
~iA
7803-51-2
CHOXD;
CHOXD;
Phosphine
CHRED; or CaRED; or
INCIN
INCIN
P102
~
107-19-7
(WETOX or FSUBS; or Propargyl alcohol
CHOXD)
Lb INCIN
CARBN; or
INCIN
P105
NA
26628-22—8
CHOXD;
FST.JBS;
Sodium azide
CHRED;
CHOXD;
CARBNI.
CHRED; or
BIODG; or INCIN
INCIN
P108
1i~
57-24-9~’
A
(WETOX or INCIN
Strychnine and salts
CHOXD)
Lb
CARBN; or
INCIN
128—872
403
P109
~fA
3689-24-5
CARBN;
or FSUBS; or Tetraethyldithio-
INCIN
INCIN
pyrophosphate
P112
1j?~,
509-14-8
CHOXD;
FSUBS;
Tetranitroinethane
CHRED;
CHOXD;
CARBN;
CHRED; or
BIODG; or INCIN
INCIN
P113
Table B
3l4-32—5
NA
RTHRM;
or Thallic oxide
STABL
P115
Table
B
7446—18—6
NA
RTHRN;
or
Thallium
(I)
sulfate
STABL
P116
NA
79-19-6
(WETOX
or
INCIN
Thioseinicarbazide
CHOXD)
Lb
CARBN;
or
INCIN
P118
~
75-70-7
(WETOX or INCIN
Trichloromethane-
CHOXD)
fb
thiol
CARBN;
or
INCIN
P119
Table B 7803-55-6
NA
STABL
Axamonium vanadate
P120
Table B 1314-62-1
NA
STABL
Vanadium
pentoxide
P122
~
1314-84-7
CHOXD;
CHOXD;
Zinc Phosphide
CHRED; or CHRED; or (4?10)
INCIN
INCIN
U001
~jA
75-07-0
(WETOX or FCUBC; or Acetaldehyde
CHOXD)
fb INCIN
CARBN;
or
INCIN
t1003
Table B 75-05-8
NA
INCIN
Acetonitrile
U006
~
75—36-5
(WETOX or INCIN
Acetyl chloride
CHOXD)
Lb
CARBN;
or
INCIN
U007
~
79-06-1
(WETOX or INCIN
Acrylamide
CHOXD)
Lb
CARBN;
or
INCIN
128—87 3
404
U008
~
79-10-7
(WETOX or FSIJBS;
or Acrylic acid
CHOXD) fb INCIN
CARBN; or
INCIN
u010
fl~
50-07-7
(WETOX or INCIN
Nitomycin C
CHOXD)
fb
CARBN;
or
INCIN
U011
~
61-82-5
(WETOX or INCIN
Amitrole
CHOXD)
fb
CARBN; or
INCIN
U014
~
492-80-8
(WETOX or INCIN
Auramine
CHCXD)
Lb
CARBN; or
INCIN
U015
~
115-02-6
(WETOX or INCIN
Azaserine
CHOXD)
fb
CARBN; or
INCIN
TJO16
~
225-51-4
(WETOX or FSUBS; or Benz
(C)
acridine
CHOXD)
fb INCIN
CARBN; or
INCIN
13017
NA
98-87-3
(WETOX or INCIN
Benzal chloride
CHOXD)
Lb
CARBN; or
INCIN
U020
~jA
98—09-9
(WETOX or INCIN
Benzenesulfonyl
CHOXD)
Lb
chloride
CARBN; or
INCIN
U021
~
92-87-5
(WETOX or INCIN
Benzidine
CHOXD)
Lb
CARBN; or
INCIN
U023
hA
98-07-7
CHOXD;
FSUBS;
Benzotrichloride
CHRED;
CHOXD;
CARBN;
CHRED; or
BIODG; or INCIN
INCIN
12 8—874
405
U026
~
494-03-1
(WETOX or INCIN
Chlornaphazin
CHOXD)
Lb
CARBN;
or
INCIN
U033
~
353-50-4
(WETOX
or INCIN
Carbonyl fluoride
CHOXD)
Lb
CARBN; or
INCIN
13034
NA
75-87-6
(WETOX or INCIN
Trichloro-
CHOXD)
Lb
acetaldehyde
CARBN; or
(Chloral)
INCIN
U035
NA
305-03-3
(WETOX or INCIN
Chlorambucil
CHOXD)
Lb
CARBN; or
INCIN
U038
Table B 510-15-6
NA
INCIN
Chlorobenzilate
13041
NA
106-89-8
(WETOX or INCIN
1-Chloro-2,3-epoxy-
CHOXD)
Lb
propane (Epichloro-
CARBN; or
hydrin)
INCIN
U042
Table B 110-75-8
NA
INCIN
2-Chloroethyl vinyl
ether
13046
~
107-30-2
(WETOX or INCIN
Chloromethyl methyl
CHOXD)
Lb
ether
CARBN; or
INCIN
U049
NA
3165-93-3
(WETOX or INCIN
4-Chloro-o-toluidine
CHOXD)
Lb
hydrochloride
CARBN;
or
INCIN
U053
~
4170-30-3
(WETOX or FSUBS; or Crotonaldehyde
CHOXD) Lb INCIN
CARBN; or
INCIN
U055
~
98-82-8
(WETOX or FSUBS; or Cumene
CHOXD) Lb INCIN
CARBN; or
INCIN
128—875
406
13056
~
110-82-7
(WETOX
or
FSUBS;
or
Cyclohexane
CHOXD)
Lb
INCIN
CARBN;
or
INCIN
U057
Table
B
108-94-1
NA
FSUBS;
or
Cyclohexanone
INCIN
13058
~
50-18-0
CARBN;
or
FST.JBS;
or Cyclophosphamide
INCIN
INCIN
13059
~
20830—81-3
(WETOX or INCIN
Daunomycin
CHOXD)
Lb
CARBN; or
INCIN
13062
ZIA
2303-16-4
(WETOX or INCIN
Diallate
CHOXD) Lb
CARBN; or
INCIN
U064
~
189—55—9
(WETOX or
FSUBS;
or
1,2,7,8—Dibenzo—
CHOXD)
Lb INCIN
pyrene
CARBN; or
INCIN
13073
~
91-94-1
(WETOX or INCIN
3,3’—Dichlorobenz-
CHOXD)
Lb
idine
CARBN;
or
INCIN
13074
hA
1476—11—5
(WETOX or INCIN
cis-1,4—Dichloro-2-
CHOXD)
Lb
butene; trans-1,4—
CARBN; or
Dichloro-2-butene
INCIN
U085
~
1464-53-5
(WETOX or FSUBS; or l,2:3,4-Diepoxy—
CHOXD)
Lb INCIN
butane
CARBN;
or
INCIN
13086
~Th
1615-80-1
CHOXD;
FSUBS;
N,N-Diethylhydrazine
CHRED;
CHOXD;
CARBNI
CHRED; or
BIODG; or INCIN
INCIN
13087
~
3288-58-2
CARBN; or FSUBS; or 0,0—Diethyl 5-
INCIN
INCIN
methyldithio-
phosphate
128—876
407
13089
~
56-53-1
(WETOX or FSUBS; or Diethyl stilbestrol
CHOXD)
Lb INCIN
CARBN;
or
INCIN
U090
~A
94-58-6
(WETOX or FSUBS; or Dihydrosafrole
CHOXD)
Lb INCIN
CARBN;
or
INCIN
U091
~
119-90-4
(WETOX or INCIN
3,3’-Dimethoxy-
CHOXD)
Lb
benzidine
CARBN; or
INCIN
13092
J1~
124-40-3
(WETOX or INCIN
Dimethylamine
CHOXD)
Lb
CARBN; or
INCIN
13093
Table B 621-90-9
NA
INCIN
p-Dimethylaminoazo-
benzene
13094
~
57-97-6
(WETOX or FSUBS; or 7,12-Dimethylbenz-
CHOXD)
Lb INCIN
(a)anthracene
CARBN; or
INCIN
13095
~
119-93-7
(WETOX or INCIN
3,3’-Diinethylbenz-
CHOXD)
Lb
idine
CARBN; or
INCIN
U096
~
80-15-9
CHOXD;
FSUBS;
alpha,alpha-
CHRED;
CHOXD;
Dimethyl-benzyl
CARBN~
CHRED;
or hydroperoxide
BIODG; or INCIN
INCIN
U097
~
79-44-7
(WETOX or INCIN
Dimethylcarbamoyl
CHOXD)
fb
chloride
CARBN; or
INCIN
13098
~
57—14-7
CHOXD;
FSUBS;
l,1—Dimethyl—
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED; or
BIODG; or INCIN
INCIN
128—87 7
408
13099
NA
540-73—8
CHOXD;
FSUBS;
1,2—Dimethyl—
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED; or
BIODG;
or
INCIN
INCIN
13103
J~A
77—78-1
CHOXD;
FSUBS;
Dimethyl sulfate
CHRED;
CHOXD;
CARBN;
CHRED; or
BIODG;
or
INCIN
INCIN
13109
hA
122—66-7
CHOXD;
FSUBS;
1,2—Diphenyl-
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED; or
BIODG; or INCIN
INCIN
Ul10
~th
142-84-7
(WETOX or INCIN
Dipropylamine
CHOXD)
Lb
CARBN;
or
INCIN
13113
hLA
140-88-5
(WETOX or FSUBS; or Ethyl acrylate
CHOXD)
Lb INCIN
CARBN;
or
INCIN
13114
~
111-54-6
(WETOX or INCIN
Ethylenebisdithio-
CHOXD)
Lb
carbamic acid
CARBN;
or
INCIN
13115
75-21-8
(WETOX or CHOXD; or Ethylene oxide
CHOXD)
Lb INCIN
CARBN;
or
INCIN
13116
hIA
96—45-7
(WETOX or INCIN
Ethylene thiourea
CHOXD)
Lb
CARBN; or
INCIN
13119
hth
62-50-0
(WETOX or INCIN
Ethyl methane-
CHOXD) Lb
sulfonate
CARBN; or
INCIN
128—878
409
13122
~
50-00-0
(WETOX
or
FSUBS;
or
Formaldehyde
CHOXD)
fb INCIN
CARBN;
or
INCIN
13123
NA
64-18-6
(WETOX or
FSUBS;
or Formic acid
CHOXD)
Lb INCIN
CARBN;
or
INCIN
13124
NA
110-00-9
(WETOX or FSTJBS; or Furan
CHOXD)
fb INCIN
CARBN; or
INCIN
U125
~
98-01-1
(WETOX or FSUBS; or Furfural
CHOXD)
Lb INCIN
CARBN; or
INCIN
U126
~
765-34-4
(WETOX or FSUBS;’ or Glycidyj~aldehyde
CHOXD)
Lb INCIN
CARBN; or
INCIN
13132
fl~
70-30-4
(WETOX
or
INCIN
Hexachlorophene
CHOXD)
Lb
CARBN; or
INCIN
U133
~
302—01-2
CHOXD;
FSUBS;
Hydrazine
CHRED;
CHOXD;
CARBN~
CHRED;
or
BIODG;
or
INCIN
INCIN
13134
Table B 7664-39-3
NA
ADGAS Lb
Hydrogen Fluoride
NEUTR; or
NEUTR
13135
~
7783-06-4
CHOXD;
CHOXD;
Hydrogen SulLide
CHRED; or CHRED; or
INCIN
INCIN
U143
~
303—34-4
(WETOX or INCIN
Lasiocarpine
CHOXD)
Lb
CARBN; or
INCIN
128—879
410
13147
~
108-31-6
(WETOX or FSUBS; or Maleic anhydride
CHOXD)
Lb INCIN
CARBN; or
INCIN
13148
hi~
123-33-1
(WETOX or INCIN
Maleic hydrazide
CHOXD)
Lb
CARBN; or
INCIN
U149
NA
109-77-3
(WETOX or INCIN
Malononitrile
CHOXD)
Lb
CARBN; or
INCIN
U150
hA
148-82-3
(WETOX or INCIN
Nelphalan
CHOXD)
fb
CARBN; or
INCIN
U151
Tables
7439-97-6
NA
RMERC
Mercury:
(High
A
& B
Mercury Sub-
category——greater
than or equal to 26
mg/kg total Mercury
13153
NA
74-93-1
(WETOX or INCIN
Methanethiol
CHOXD)
Lb
CARBN; or
INCIN
13154
NA
67-56-1
(WETOX or FSUBS; or Methanol
CHOXD)
Lb INCIN
CARBN; or
INCIN
13156
~
79-22-1
(WETOX or INCIN
Methyl chloro-
CHOXD)
Lb
carbonate
CARBN; or
INCIN
13160
NA
133’8-23-4
CHOXD;
FSUBS;
Methyl ethyl ketone
CHRED;
CHOXD;
peroxide
CARBN~
CHRED;
or
BIODG; or INCIN
INCIN
13163
~
70-25-7
(WETOX or INCIN
N-Nethyl-N’-nitro-N-
CHOXD)
Lb
Nitrosoguanidine
CARBN;
or
INCIN
128—880
411
U164
~
56-04-2
(WETOX or INCIN
Methyithiouracil
CHOXD)
Lb
CARBN; or
INCIN
U166
~
130-15-4
(WETOX or FSUBS; or 1,4—Naphthoquinone
CHOXD)
Lb INCIN
CARBN; or
INCIN
13167
hA
134-32-7
(WETOX or INCIN
1-Naphthylamin~
CHOXD)
Lb
CARBN; or
INCIN
13168
Table B 91-59-8
NA
INCIN
2-Naphthylaiuine
13171
NA
79-46-9
(WETOX or INCIN
2-Nitropropane
CHOXD)
Lb
CARBN; or
INCIN
13173
NA
1116-54-7
(WETOX or INCIN
N-Nitroso-diethanol-
CHOXD)
Lb
amine
CARBN;
or
INCIN
13176
~iA
759-73-9
(WETOX or INCIN
N-Nitroso-N-ethyl-
CHOXD)
Lb
urea
CARBN; or
INCIN
13177
NA
684-93-5
(WETOX or INCIN
N-Nitroso-N-methyl-
CHOXD)
Lb
urea
CARBN; or
INCIN
13178
~A
615-53-2
(WETOX or INCIN
N-Nitroso-N-methyl-
CHOXD)
fb
urethane
CARBN; or
INCIN
13182
~
123—63-7
(WETOX or FSUBS; or Paraldehyde
CHOXD)
Lb INCIN
CARBN; or
INCIN
U184
~
76-01-7
(WETOX or INCIN
Pentachloroethane
CHOXD)
Lb
CARBN;
or
INCIN
128—88 1
412
U186
~
504-60-9
(WETOX or FSUBS; or 1,3—Pentadiene
CHOXD) Lb INCIN
CARBN; or
INCIN
U189 j~
1314-80-3
CHOXD;
CHOXD;
Phosphorus sulfide
CHRED; or CHRED; or
INCIN
INCIN
U191
~
109-06—8
(WETOX or INCIN
2-Picoline
CHOXD)
Lb
CARBN; or
INCIN
U193
~
1120-71-4
(WETOX or INCIN
1,3—Propane sultone
CHOXD)
Lb
CARBN;
or
INCIN
U194
~
107-10-8
(WETOX or INCIN
n-Propylamine
CHOXD)
Lb
CARBN; or
INCIN
13197
~
106-51-4
(WETOX or FSUBS; or p-Benzoquinone
CHOXD)
Lb INCIN
CARBN; or
INCIN
U200
NA
50-55-5
(WETOX or INCIN
Reserpine
CHOXD)
Lb
CARBN; or
INCIN
13201
hA
108-46-3
(WETOX or FSUBS; or Resorcinol
CHOXD)
Lb INCIN
CARBN; or
INCIN
13202
~
81-07-2k
~
(WETOX or INCIN
Saccharin and salts
CHOXD)
Lb
CARBN; or
INCIN
13206
~
18883-66-4
(WETOX or INCIN
Streptozatocin
CHOXD)
Lb
CARBN;
or
INCIN
12 8—882
413
U213
~
109-99-9
(WETOX or FSUBS; or Tetrahydrofuran
CHOXD)
Lb INCIN
CARBN; or
INCIN
13214
Table B 563—68—8
NA
RTHRM;
or Thallium
(I) acetate
STABL
U215
Table B 6533-73-9
NA
RTHRZ4;
or Thallium
(I)
STABL
carbonate
13216
Table B 7791-12-0
NA
RTHRM; or Thallium
(I)
STABL
chloride
U2l7
Table B 10102—45—1 NA
RTHRN;
or Thallium
(I) nitrate
STABL
13218
~
62-55-5
(WETOX or INCIN
Thioacetamide
CHOXD)
Lb
CARBN; or
INCIN
13219
NA
62-56-6
(WETOX or INCIN
Thiourea
CHOXD)
Lb
CARBN; or
INCIN
U221
NA
25376-45-8 CARBN; or FSUBS;
or Toluenediamine
INCIN
INCIN
13222
hA
636-21-5
(WETOX or INCIN
o-Toluidine hydro-
CHOXD)
Lb
chloride
CARBN; or
INCIN
U223
h!A
26471-62-5 CARBN; or FSUBS; or Toluene diisocyanate
INCIN
INCIN
13234
hi~
99-35-4
(WETOX or INCIN
sym-Trinitrobenzene
CHOXD)
Lb
CARBN; or
INCIN
13236
~
72-57-1
(WETOX or INCIN
Trypan Blue
CHOXD)
Lb
CARBN; or
INCIN
128—883
414
13237
hA
66-75-1
(WETOX or INCIN
Uracil mustard
CHOXD)
Lb
CARBN; or
INCIN
13238
~
51-79-6
(WETOX or INCIN
Ethyl carbamate
CHOXD)
Lb
CARBN; or
INCIN
13240
hA
94-75-7k
A
(WETOX or INCIN
2,4-Dichiorophenoxy-
CHOXD)
Lb
acetic acid
(salts
cA.RBN; or
and esters)
INCIN
U244
NA
137-26-8
(WETOX or INCIN
Thiram
CHOXD)
fb
CARBN; or
INCIN
13246
~
506-68-3
CHOXD;
CHOXD;
Cyanogen bromide
WETOX; or WETOX; or
INCIN
INCIN
13248
~
81-81-2
(WETOX or FSUBS; or Warfarin (greater
CHOXD)
Lb INCIN
than or equal to 3
CARBN; or
or less)
INCIN
13249
~IA
1314-84-7
CHOXD;
CHOXD;
Zinc Phosphide
CHRED; or CHRED; or
(10)
INCIN
INCIN
~A
CAS Number given for parent compound only.
~
This waste code exists
in gaseous form and is not
categorized as wastewater or nonwastewater forms.
NA
Not Applicable.
BOARD NOTE:
When a combination of these technologies
(i.e., a
treatment train)
is specified as a single treatment standard, the
order of application is specified in this Table by indicating the
five letter technology code that must be applied first, then the
designation “Lb”
(an abbreviation for “Followed by”), then the
five letter technology code Lor the technology that must be
applied next, and so on.
When more than one technology
(or
treatment train)
are specified a alternative treatment standards,
the five letter technology codes
(or the treatment trains) are
separated by a semicolon
(;)
with the last technology preceded by
the word
“or”.
This indicates that any one of these BDAT
technologies or treatment trains can be used Lor compliance with
128—8 84
415
the standard.
See Section 728.Table C for a listing of the
technology codes and technology—based treatment standards.
Derived from 40
CFR
268.42, Table
2,
as adopted at 54
Fed.
flcg.
22694, June
1,
1990
(1990).
as amended at 56
Fed. Req.
3876.
January 31,
1991.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
Section
728.Table
E
Standards for Radioactive Mixed Waste
tmECIINOLOCY
CODE
WACTE
z~iuzi
WACTE uiii~riurit~
AND/OR
CODEC
CAD
NO.
WACTEWATERS
WACTEWATERCTREATNENT
CUBCATEGORY
D002 NA
NA
HLVIT
Radioactive High Level Wastes
Cenerated During the
Reprocessing oL Fuel Rods
Cubeategory
D004 NA
NA
HLVIT
Radioactive High Level Wastes
Cenerated During the
Reprocessing of Fuel Rods
Cubccitegory
D005 NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the
Reprocessing oL Fuel Rods
Cubcategory
D006 NA
NA
HLVIT
Radioactive
High
Level
Wastes
Cenerated During the
Reprocessing of Fuel Rods
Cubcategory
D007
NA
NA
HLVIT
Radioactive High Level Wastes
Cenerated During the
aeprocessing of Fuei
ioas
Cubcategory
Radioactive Lead Colids
~uDcategory
(Note: these
.LCUQ
solids include, but are not
limited to, all forms of lead
shielding,
and other elemental
forms
of lead. These lead
solids do not include
treatment residual
~arox.ac
si.udges,
128—885
416
residuals,
-or incinerator
ashes that can undergo con
vcntional
ata?ilizat
pozzolanic
do
ion, nor
they
tnat can be incinerated and
stabilized as ash.)
D000 NA
NA
IILVIT
Radioactive High Level Wastes
the
Ccneratcd During
Reprocessing of
Cubcategory
Fuel Rods
D009 7439
97
6
NA
AMLGN
Elemental
i~t-~~r
with radioactive materials
T-Twiraujjc
pu.
contaminateu
tJ’i1r~
Mvi~iii~j
Radioactive
Materials Cubcatcgory
D009
NA
NA
HLVIT
Radioactive High Level Wastes
Cencrated Durimg the
Reprocessing of
Fuel
Rods
Cubcategory
DOlO NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the
Reprocessing of Fuel Rods
Cubcategory
DOll NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the
Reprocessing of Fuel Rods
Cubcategory
U15l 7430
97
6
NA
ANLCM
Mercury: Elamenta~.mercury
contaminated with radioactive
materials
NA -Not Applicable.
Technotogy Code
Waste code
Waste descriptthns and/or
CAS
No.
Wastewaters
Nonwastewaters
treatment cateqory
0002
Radioactive high tevet
NA
NA
wastes
generated
~jring
the
reprocessing
of
fuet
rods s~.tcategory
128—886
417
D004
Radioactive high level
~
wastes
generated during
the
reprocessing
of
fuel
rods s’Acateqory
D005
Radioactive high
level
NA
NA
HLVIT
wastes
generated
during
the
reprocessing
of
fuel
rods
s~tcategory
0006
Radioactive high level
NA
NA
HLVIT
wastes
generated during
the reprocessing of
fuel
rods
st*xategory
D007
Radioactive high Level
HA
HLVIT
wastes
generated during
the
reprocessing
of
fueL
rods
subcategory
0008
Radioactive lead soLids
7439-92-1
HA
MACRO
subcategory (Note: these
Lead solids
include, but
are
not
Limited
to.
aLl
forms
of
Lead shielding.
and other elemental forms
of
lead.
These
Lead
solids
do
not
include
treatment residuals such
as
hydroxide
sludges.~
other wastewater
treatment
residuals,
or
incinerator
ashes
that
can
~s~dergo
conventional
~lanicstabilization.
nor
do they
include
organolead materials that
can
be
incinerated and
stabilized as ash).
0008
Radioactive high level
NA
NA
HLVIT
wastes generated during
the
reprocessing
of
fuel
rods subcategory
D009
Elemental mercury
7439-97-6
contaminated with
radioactive materials
D009
Hydraulic oiL
7439-97-6
contaminated
with
mercury; radioactive
materials
si.Ecateqory
0009
Radioactive high Level
NA
!IbYAI
wastes
generated
during
the reprocessing of
fuel
rods
si.E,category
0010
Radioactive
high
level
NA
wastes
generated
during
the reprocessing of
fuel
rods
sthcategory
128—887
418
Doll
Radioactive high level
NA
NA
HLVIT
wastes
generated during
the reprocessing of fuel
rods
subcategory
11151
Mercury: Elemental
7439-97-6
mercurY
contaminated
with
radioactive materials
Note: NA
means
Not AppLicable.
(Source:
Amended at 16 Ill. Reg.
,
effective
)
128—888
